TW200831278A - Roll of polyolefin microporous film and the producing method thereof - Google Patents

Roll of polyolefin microporous film and the producing method thereof Download PDF

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Publication number
TW200831278A
TW200831278A TW096127108A TW96127108A TW200831278A TW 200831278 A TW200831278 A TW 200831278A TW 096127108 A TW096127108 A TW 096127108A TW 96127108 A TW96127108 A TW 96127108A TW 200831278 A TW200831278 A TW 200831278A
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Taiwan
Prior art keywords
winding
wound
polyolefin microporous
film
less
Prior art date
Application number
TW096127108A
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Chinese (zh)
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TWI334825B (en
Inventor
Yoshifumi Nishimura
Akira Takahashi
Yasushi Niihara
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Asahi Kasei Chemicals Corp
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Publication of TW200831278A publication Critical patent/TW200831278A/en
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Publication of TWI334825B publication Critical patent/TWI334825B/zh

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/28Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a liquid phase from a macromolecular composition or article, e.g. drying of coagulum
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/22After-treatment of expandable particles; Forming foamed products
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/04Construction or manufacture in general
    • H01M10/0404Machines for assembling batteries
    • H01M10/0409Machines for assembling batteries for cells with wound electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • H01M10/0587Construction or manufacture of accumulators having only wound construction elements, i.e. wound positive electrodes, wound negative electrodes and wound separators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/403Manufacturing processes of separators, membranes or diaphragms
    • H01M50/406Moulding; Embossing; Cutting
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/411Organic material
    • H01M50/414Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/417Polyolefins
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H01M50/491Porosity
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • H01M50/494Tensile strength
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Cell Separators (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

A roll of polyolefin microporous film consisting of a roll having a polyolefin microporous film rolled up around a roll core, characterized in that the absolute value ([μm) of difference (film thickness difference) between the film thickness (T, [μm) calculated according to the formula (1) and the film thickness (t, [μm) evaluated for one sheet is 1.5 [mu]m or less. Further, there is provided a process for producing the same. T(μm) = π (D2-d2)/4L (1) wherein D is the outer diameter (mm) of roll resulting from rolling up around the roll core including the porous film; d the outer diameter (mm) of roll core; and L the length rolled up (m) of the roll.

Description

200831278 九、發明說明: 【發明所屬之技術領域】 本發明係關於一種使用於電池隔離膜之聚烯烴製微多孔 膜捲繞物,亦即,將聚烯烴或含有聚烯烴之樹脂組合物所 構成之微多孔膜捲繞於卷芯上所成者。本發明係關於一種 尤其可較好地用作鋰離子二次電池用隔離膜的聚烯烴製微 多孔膜捲繞物及其製造方法 【先前技術】 聚烯烴製微多孔膜被用作各種電池用隔離膜。尤其是, 由於聚烯烴樹脂對有機溶劑之耐性優異,且電絕緣性亦優 異等,故特別多地應用於鐘離子二次電池中。 近年來’伴隨鋰離子二次電池之主要用途即行動電話或 電月® 以及其他便攜式機器的多功能化、輕量化、低成本 化5進一步要求電池高容量化、高能量密度化。其中,針 對雨各量化、高能量化,要求隔離膜薄膜化。另一方面, 因為將同時捲繞有隔離膜及電極之捲繞物(電極•隔離膜 捲繞物)裝入至電池之外殼中,故要求電極•隔離膜捲繞 物之外徑精度較好。 最近亦研究了將大型鐘離子二次電池使用於汽車 用、儲藏用之用途中,此時所使用之隔離膜係寬度較寬、 卷長較長者。為擴大如此之大型鋰離子二次電池之普及, 亦必須可高精度地製作捲繞物之外徑,降低插入外殼時之 不良率,實現低成本化。 例如’專利文獻1中,提出有為提昇製造電池隔離膜等 123124.doc 200831278 時之作業性等’而將最大外徑及最小外徑控制在特定範圍 内的聚烯烴製微$ $腊植& & ^ ^ , 1 夕孔膜捲繞物。然而,上述捲繞物之外徑 精度並不充分。 專利文獻1:日本專利特開2004-99799號公報 【發明内容】 發明所欲解決之問題 本發明之目的在於提供一種可降低將電極•隔離膜捲繞200831278 IX. Description of the Invention: [Technical Field] The present invention relates to a polyolefin microporous film winding for use in a battery separator, that is, a polyolefin or a polyolefin-containing resin composition. The microporous membrane is wound around the core. The present invention relates to a polyolefin microporous film winding which is particularly preferably used as a separator for a lithium ion secondary battery and a method for producing the same. [Prior Art] A polyolefin microporous film is used for various batteries. Isolation membrane. In particular, polyolefin resins are particularly useful in clock ion secondary batteries because of their excellent resistance to organic solvents and excellent electrical insulating properties. In recent years, the use of mobile phones, electric moons, and other portable devices, which are the main applications of lithium ion secondary batteries, has become more versatile, lighter, and more cost-effective. Among them, the rain is quantified and the energy is increased, and the separator film is required to be thinned. On the other hand, since the winding film (electrode/spacer winding) in which the separator and the electrode are wound at the same time is loaded into the outer casing of the battery, the outer diameter of the electrode/spacer winding is required to be excellent. . Recently, large-sized plasma ion secondary batteries have been studied for use in automobiles and storage applications, and the separators used at this time have a wide width and a long coil length. In order to expand the spread of such large-sized lithium ion secondary batteries, it is necessary to produce the outer diameter of the wound material with high precision, and to reduce the defective rate when inserting the outer casing, thereby achieving cost reduction. For example, in the case of the patent document 1, it is proposed to increase the maximum outer diameter and the minimum outer diameter to a specific range in order to improve the workability of manufacturing a battery separator, such as 123124.doc 200831278, etc. ; & ^ ^ , 1 etching film. However, the outer diameter accuracy of the above-mentioned winding is not sufficient. Patent Document 1: Japanese Patent Laid-Open No. 2004-99799 SUMMARY OF INVENTION Technical Problem An object of the present invention is to provide a method for reducing winding of an electrode/separator

物插入外殼時產生之插入不良的聚烯烴製微多孔膜捲繞 物進而本發明之目的在於提供一種可利用電極•隔離 膜捲繞物之外徑而進行厚度控制的聚烯烴製微多孔膜捲繞 物及其製造方法。 解決問題之技術手段 本發明者等人不僅著眼於提高電極•隔離膜捲繞物之外 徑精度’極其重要的是控制作為其材料之聚烯烴製微多孔 膜(隔離膜)捲繞物之外徑精度,且對上述事項進行了銳意 研究,結果發現了可解決上述問題之方法,從而完成本發 明。尤其是’發現:利用根據日本專利特開2〇〇6-88255號 公報中所揭示之切割輥外徑測量機所測量之外徑及卷長而 計算出的厚度資訊,可高精度地控制與電極一併捲繞之捲 繞物的外徑,從而完成本發明。 又,本發明者等人發現,於對捲繞於母輥(切割成所需 寬度之前之輥)上之聚烯烴製微多孔膜,於其總寬度上切 割成特定寬度後,捲取所切割出之各聚烯烴微多孔膜而製 成捲繞物之情形時,為提高捲繞物之外徑精度,只要對各 123124.doc 200831278 捲繞物之捲取張力加以控制即可。 即,先前,於對捲繞於母輥上之聚烯烴製微多孔膜,於 其總寬度上將其切割成特定寬度後,捲取所切割出的各聚 烯烴製微多孔膜捲繞物而製造成捲繞物之情形時,可將所 捲繞之複數個捲繞物作為整體而同時控制各聚烯烴製微多 孔膜之捲取張力、或相應於特定之捲繞物而將所有聚烯烴 製微多孔膜之捲取張力控制為均一,根據本發明者等人之 研究,判斷出:於如此之控制方法中,並非單獨控制之對 象之捲繞物會捲繞得較緊或捲繞較鬆,無法控制其外徑。 即,本發明如下所述。 一種聚烯烴製微多孔膜捲繞物,其特徵在於:其係將聚 _煙製微多孔膜捲繞於卷芯上之捲繞物,且根據下述式(1 ) 所計算出之膜厚Τ(μπι)與對一片所評估出之膜厚ί(μιη)之差 (膜厚差)的絕對值(μχη)為1 ·5 μιη以下, T(pm)=7i(D2-d2)/4L (1) (上述式(1)中,D係指捲繞於卷芯上之包含多孔膜之捲繞 物的外徑(mm),d係指卷芯之外徑(mm),L係指捲繞物之 卷長(m))。 又,本發明如下所述。 一種聚烯烴製微多孔膜捲繞物之製造方法,其包括以下 步驟: 對捲繞於母輥上之聚烯烴製微多孔膜,於其總寬度上切 割成特定寬度;以及 一面控制由切割成該特定寬度之各聚烯烴製微多孔膜所 123124.doc 200831278 構成之各捲繞物的捲取張力,一面進行捲繞。 發明之效果 若使用本發明之聚烯烴製微多孔膜捲繞物,則可製造出 • 插入外殼時之插入不良較少之電極•隔離膜一體型捲繞 物。進而,根據本發明,可利用電極•隔離膜一體型捲繞 物之外徑而進行厚度控制。又,本發明之製造方法可高效 ‘ 地製造上述聚烯烴製微多孔膜捲繞物。若將本發明之方法 • 應用於電極等中,進而亦可準確地進行電極•隔離膜_體 型捲繞物之外徑控制。 【實施方式】 以下,詳細說明本發明。 [5^稀煙製微多孔膜捲繞物] 本發明之聚烯烴製微多孔膜捲繞物之特徵在於:其係將 聚烯烴製微多孔膜捲繞於管等圓柱狀卷芯上之捲繞物,且 根據下述式(1)所計算出之膜厚Τ(μιη)與對一片所評估出之 馨 膜尽t(^m)的差(膜厚差)的絕對值(μπι)為1 ·5 μπι以下, T(pm)=7i:(D2-d2)/4L ⑴ (上述式(1)中,D係指捲繞於卷芯上之包含多孔膜之捲繞 物的外桎(mm) ’ d係指卷芯之外徑(mm),l係指捲繞物之 -, 卷長(m))。 • 當膜厚之差(Tet)大於15 μηι時,由於捲繞物之捲繞過 鬆,故而使得於將其用作電極•隔離膜捲繞物之情形時, 無法進行電極•隔離膜捲繞物之外徑控制,當插入外殼 時,無法插入等不良問題將會增多。另一方面,當膜厚之 123124.doc 200831278 差(T-t)小於·1·5 μπι時,由於捲繞物之捲繞過緊,故導致捲 繞物之透過性不良,膜厚之差之絕對值較好的是1 ·2 μιη以 下,更好的是1 · 0 μιη以下,最好的是0.5 μπι以下。 膜厚之差(T-t)之絕對值小得越接近於〇,則聚烯烴製微 多孔膜越不會出現捲繞鬆弛或捲繞緊繃,本發明中,聚烯 烴製微多孔膜捲繞物較好的是稍稍緊繃捲繞。具體而言, 較好的是T-t之值(μιη)為-〇.5$T-t<0。 再者,本發明中,所謂「卷芯」,係將聚烯烴製微多孔 丨 膜製作成捲繞物時所使用的芯體,係指圓柱形狀者。作為 較好之具體例’可列舉紙管、塑料管等管。 就減少將電極•隔離膜捲繞物插入外殼時之插入不良的 方面考慮,本發明之較好態樣為如下所述之聚烯烴製微多 孔膜捲繞物群:其係包含2個以上之由切割捲繞於母輥上 之聚烯fe製微多孔膜所得的上述聚烯烴製微多孔膜捲繞物 的捲繞物群,捲繞偏移為5 mm以内,且上述膜厚之差(pm) 丨 之標準偏差為〇·7 μιη以下,進而為〇·5 μιη以下。此處,所 謂母輥,係指切割成使用者所需之寬度之前的輥,通常, 寬度為350 mm以上,進而為6〇〇 mm以上。所謂捲繞偏 移,係指將聚烯烴製微多孔膜捲繞於卷芯上之捲繞物中, •於所捲繞之聚烯烴微多孔膜之總長上,所捲繞之聚烯烴微 _ 多孔膜之端部的位置偏移。亦即,所捲繞之聚烯烴微多孔 膜之-端部的位於捲繞物《寬度方向冑外側的部分與位於 j内侧的部分之間在寬度方向上的距離。進而,不僅對於 單獨之捲燒物而言,而且對於構成母概總寬度之複數個捲 123124.doc 200831278 物(捲繞物群)而言,勿庸置疑較好的均是膜厚之差較 小 〇 本發明中’所謂「捲繞於卷芯上之包含多孔膜之捲繞物 的外k」D,係指當使將聚烯烴製微多孔膜捲繞於軸上之 . 聚烯文工製械多孔膜捲繞物形成為圓柱形時的直徑,於其叫 面並非正圓之情形時,設該「捲繞於卷芯上之包含多孔媒 之捲繞物的外獲」〇為與剖面外切之面積最小的外切長方 • 开》之短邊舆長邊的平均值。具體而言,可藉由下述方法而 、、出對於相距捲繞物之兩端3腿以上之靠内側的部分, 使用如下所述之方法,於沿微多孔膜之寬度方向等間隔之 複數個位置處,測量捲繞物之直徑,計算出其平均值。 本發明之聚稀烴製微多孔膜捲繞物之外徑D,例如可藉 由如圖1所示之日本專利特開2006·88255號公報中所記^ 料徑測!裝置而高精度且高效率地測量。圖!係表示測 量捲繞物外徑之機構的基本構成部分之概略圖。即,為光 •機職受由投影機1Α投射之雷射或可見光,測量捲繞物2 之影像’猎此測量捲繞物之外徑。該等投影機、受光機可 使用通常市售之作為雷射尺寸測量機、或數位尺寸測量機 等者。 • 例如’使包含2組投影機_受光機㈣尺寸測量裝置 •沿捲繞物2之旋轉轴方向平行移動,藉此,於線上測量捲 繞物^旋轉抽(卷芯)方向之所有位置上的外徑。若為使尺 寸測置裝置對於捲繞物2而相對移動,則可移動尺寸測量 裝置且可移動捲繞物2。又,根據所測量之捲繞物的不 123124.doc 11 200831278 同,有時考磨 ^到操作性亦可將捲繞物橫置等而製作出測量 ;可新摅投影機、受光機所構成之尺寸測量裝置的移動速 :。:所需之捲繞物之測量精度、測量時間等而適當確 外“之测量可對外切長方形之短邊及長邊所對 應之2方向推你 旦n 其平均值,通f,對於藉由尺寸測 仃測量之捲繞物2的測量範圍而言,只要連續測量 捲繞物之1個杨罢老, J ^ 個位置處之外徑則已充分。其理由在於,捲繞The polyolefin microporous film winding which is inserted into the outer casing and which is poorly inserted is further provided. The object of the present invention is to provide a polyolefin microporous film roll which can be controlled by the outer diameter of the electrode/spacer winding. Wrap and its manufacturing method. MEANS FOR SOLVING THE PROBLEMS The inventors of the present invention have not only focused on improving the outer diameter accuracy of the electrode/spacer winding, but it is extremely important to control the polyolefin microporous film (isolation film) wound material as a material thereof. The accuracy of the diameter and the above-mentioned matters have been intensively studied, and as a result, a method for solving the above problems has been found, thereby completing the present invention. In particular, it has been found that the thickness information calculated by the outer diameter and the coil length measured by the cutter roll outer diameter measuring machine disclosed in Japanese Laid-Open Patent Publication No. Hei. The outer diameter of the winding of the electrode is wound together, thereby completing the present invention. Further, the inventors of the present invention have found that the polyolefin microporous film wound on a mother roll (rolled before being cut into a desired width) is cut into a specific width over the total width thereof, and then taken up by winding. In the case where each of the polyolefin microporous membranes is formed into a wound material, in order to improve the outer diameter precision of the wound material, the winding tension of each of the 123124.doc 200831278 windings may be controlled. That is, previously, the polyolefin microporous film wound on the mother roll is cut into a specific width over the entire width thereof, and then the cut polyolefin microporous film windings are taken up. In the case of being wound into a wound, the wound windings may be controlled as a whole while controlling the take-up tension of each polyolefin microporous film or all polyolefins corresponding to a specific winding. The winding tension of the microporous film is controlled to be uniform. According to the study by the inventors of the present invention, it is judged that in such a control method, the winding of the object which is not separately controlled is wound tightly or wound. Loose, unable to control its outer diameter. That is, the present invention is as follows. A polyolefin microporous film wound, which is obtained by winding a poly-smoke microporous film on a winding core, and having a film thickness calculated according to the following formula (1) The absolute value (μχη) of the difference (film thickness difference) between Τ(μπι) and the film thickness ί(μιη) evaluated for one piece is 1·5 μηη or less, T(pm)=7i(D2-d2)/4L (1) (In the above formula (1), D means the outer diameter (mm) of the wound containing the porous film wound on the core, d means the outer diameter (mm) of the core, and L means The length of the winding (m)). Further, the present invention is as follows. A method for producing a polyolefin microporous film wound, comprising the steps of: cutting a polyolefin microporous film wound on a mother roll to a specific width over a total width thereof; and controlling the cutting by one side Each of the polyolefin-made microporous membranes of the specific width 123124.doc 200831278 has a winding tension of each of the wound materials and is wound. EFFECTS OF THE INVENTION When the polyolefin microporous film wound material of the present invention is used, it is possible to manufacture an electrode/spacer integrated winding which has less insertion failure when inserted into a casing. Further, according to the present invention, the thickness can be controlled by the outer diameter of the electrode/spacer integrated type wound material. Further, the production method of the present invention can efficiently produce the above-mentioned polyolefin microporous film wound material. When the method of the present invention is applied to an electrode or the like, the outer diameter control of the electrode/spacer _ body winding can be accurately performed. [Embodiment] Hereinafter, the present invention will be described in detail. [5. Thin-porous microporous film wound product] The polyolefin microporous film wound of the present invention is characterized in that a polyolefin microporous film is wound around a cylindrical core such as a tube. The absolute value (μπι) of the difference between the film thickness μ(μιη) calculated according to the following formula (1) and the scented film t(^m) evaluated for one piece (the film thickness difference) is 1 ·5 μπι or less, T(pm)=7i:(D2-d2)/4L (1) (In the above formula (1), D means the outer enthalpy of the wound containing the porous film wound around the core ( Mm) ' d is the outer diameter (mm) of the core, and l is the winding - (volume length (m)). • When the difference in film thickness (Tet) is more than 15 μηι, the winding of the wound material is too loose, so that when it is used as an electrode/separator winding, the electrode/spacer winding cannot be performed. The outer diameter of the object is controlled, and when it is inserted into the outer casing, problems such as the inability to insert may increase. On the other hand, when the film thickness 123124.doc 200831278 difference (Tt) is less than ·1·5 μπι, the winding of the wound material is too tight, resulting in poor permeability of the wound material and absolute difference in film thickness. The value is preferably 1 · 2 μηη or less, more preferably 1 · 0 μηη or less, and most preferably 0.5 μπι or less. The closer the absolute value of the difference in film thickness (Tt) is to the enthalpy, the less the looseness of the polyolefin or the tightness of the winding of the polyolefin microporous film. In the present invention, the polyolefin microporous film winding It is preferred to wind it slightly tightly. Specifically, it is preferred that the value of T-t (μιη) is -〇.5$T-t<0. In the present invention, the "core" is a core used when the polyolefin microporous film is formed into a wound, and is referred to as a cylindrical shape. As a preferable specific example, a tube such as a paper tube or a plastic tube can be cited. In order to reduce the insertion failure when the electrode/separator winding is inserted into the outer casing, a preferred aspect of the present invention is a polyolefin microporous film winding group as described below: it contains two or more The winding group of the above-mentioned polyolefin microporous film wound obtained by cutting the microporous film made of the polyene film wound on the mother roll, the winding deviation is within 5 mm, and the difference in film thickness ( Pm) The standard deviation of 丨 is 〇·7 μηη or less, and further 〇·5 μιη or less. Here, the term "master roll" refers to a roll that is cut to a width required by the user, and generally has a width of 350 mm or more and further 6 〇〇 mm or more. The winding offset refers to winding a polyolefin microporous film on a winding of a core, and on the total length of the wound polyolefin microporous film, the wound polyolefin micro_ The position of the end of the porous film is shifted. That is, the end portion of the wound polyolefin microporous film is located in the width direction between the portion of the winding "the outer side in the width direction" and the portion located inside the j. Furthermore, it is undoubtedly better that the difference in film thickness is not only for a single package but also for a plurality of rolls 123124.doc 200831278 (winding group) which constitute the total width of the mother. In the present invention, the term "the outer k"D of the wound material comprising the porous film wound on the core refers to the winding of the polyolefin microporous film on the shaft. When the mechanical porous film winding is formed into a cylindrical shape, when the surface is not a perfect circle, the "winding of the wound containing the porous medium wound on the core" is set to The average of the long side of the short side of the cut outer section of the section. Specifically, by the following method, the inner side of the three or more legs at both ends of the wound material can be used, and the method described below can be used at equal intervals along the width direction of the microporous film. At each position, the diameter of the winding is measured and the average value is calculated. The outer diameter D of the polyurea-made microporous film wound of the present invention can be measured, for example, by the measurement in Japanese Patent Laid-Open Publication No. 2006-88255. The device is measured with high precision and high efficiency. Fig.: is a schematic view showing a basic configuration of a mechanism for measuring the outer diameter of the winding. That is, for the laser or the visible light projected by the projector 1 光, the image of the winding 2 is measured and the outer diameter of the winding is measured. As such projectors and receivers, a commercially available laser size measuring machine or a digital size measuring machine can be used. • For example, 'Make 2 sets of projectors_receivers (4) size measuring devices • Move in parallel along the direction of the axis of rotation of the winding 2, thereby measuring all the positions of the windings in the direction of the winding (core) on the line The outer diameter. If the size measuring device is relatively moved with respect to the winding 2, the size measuring device can be moved and the winding 2 can be moved. In addition, according to the measurement of the winding material, 123124.doc 11 200831278, it is possible to make the measurement by traversing the winding material, etc., and it is possible to make a measurement by a new projector or a light receiver. The moving speed of the size measuring device: : The measurement accuracy, measurement time, etc. of the required winding material are properly determined. "The measurement can be performed by cutting the short side of the rectangle and the 2 directions corresponding to the long side. In terms of the measurement range of the winding 2 measured by the size measurement, as long as one of the wounds is continuously measured, the outer diameter at the J ^ position is sufficient. The reason is that the winding

物之外徑差係因將多片具有厚度差之薄膜重疊而產苴 剖面實質P焱T问 A /、 、、上马正囡,無論於何位置處進行測量,其 幾乎相等。 二 又,如圖2所示,表示測量本發明之捲繞物群之外徑時 的車乂好之例示。為使尺寸測量機高精度運轉,較好的是 將捲%物群设置於2組受光機1A及受光機⑶的大致中央 邛,例如,可於2組受光機1A及受光機1B的中央處設置用 以固定切割輥之轴等,藉由此等方式可將捲繞物群固定。 若移動2組受光機1A及受光機1B之寬度,則亦可同時對由 直徑不同之捲繞物所構成之捲繞物群進行測量。圖3中表 示有同時測量如此之由複數個捲繞物所構成之捲繞物群所 得的結果之一例。圖中之A部分係捲繞物間之間隙的測量 資料,且較理想的是具備計算處理部,其連續地自複數個 捲繞物間之連續測量資料中消去各捲繞物間之斷續部分。 為此’可採用下述方法:藉由去掉測量資料之上升、下降 之測I資料,而计异出複數個捲繞物外徑的計算方法;或 藉由對測量資料進行微分處理,去掉外徑測量產生急遽變 123124.doc -12· 200831278 化之部分’而計算出複數個捲繞物外程的計算方 , 由於當切割時分成條之情形時 ’ 捲、兀軸上’故而較理想的是具備處理部,' 測量資訊與薄膜捲繞物之膜條之 .^^ ^ 肤序貝訊的位置關係一致,並作 資料之顯示機構。 專裝置中亦可具備測量The difference in the outer diameter of the material is due to the overlapping of a plurality of films having a difference in thickness. The profile of the profile P焱T is a/, and is immediately equal to the measurement, which is almost equal regardless of the position. Further, as shown in Fig. 2, an example of the rut when measuring the outer diameter of the winding group of the present invention is shown. In order to operate the dimension measuring machine with high precision, it is preferable to arrange the volume group of objects in the center of the two sets of the light receiving machine 1A and the light receiving machine (3), for example, at the center of the two sets of the light receiving machine 1A and the light receiving machine 1B. A shaft or the like for fixing the cutting roller is provided, whereby the winding group can be fixed by such a method. When the widths of the two sets of the light receiver 1A and the light receiver 1B are moved, it is also possible to simultaneously measure the group of windings composed of the wounds having different diameters. Fig. 3 shows an example of the result of simultaneously measuring such a group of windings composed of a plurality of windings. Part A of the figure is a measurement of the gap between the windings, and preferably has a calculation processing unit that continuously eliminates the discontinuity between the windings from the continuous measurement data between the plurality of windings. section. To this end, the following method can be used: by removing the measured I data of the rise and fall of the measured data, the calculation method of the outer diameter of the plurality of windings is calculated; or by differentially processing the measured data, the external data is removed. The diameter measurement produces a sharp change 123124.doc -12· 200831278 part of the 'calculation of the calculation of the outer winding of a plurality of windings, because it is ideal when it is divided into strips when cutting. It is equipped with a processing unit, 'measurement information and the film strip of the film winding. ^^ ^ The positional relationship of the skin order Beixun is the same, and the information display mechanism. Measurements are also available in the device

=明所謂「對—片所評估出之臈厚t」,係 :、、,聚婦煙製微多孔膜的膜厚t,例如可藉由下述方 :而求出二對聚烯烴製微多孔膜捲繞物之最外周的微多孔 J ’於沿寬度方向等間隔之複數個位置處測量膜厚,並計 鼻出其平均值9 本發明中,對聚稀烴製微多孔膜之膜厚之測量方法並盈 限定,例如,除下述實施例中所示之方法以外,亦可藉由 =下所述之方法而高精度地測量,即,將測量端子^於 微夕孔膜上,讀取其動作,並換算成膜厚。測量端子之動 作之讀取過程中,例如可使用光學偵測器。又,較好的 是,將因測量端子而使微多孔膜所承载之每一單位面積之 壓力,控制在固定範圍内。進而,較好的是於恆溫室令進 行測量。 圖6係表示用以測量微多孔膜之膜厚t之裝置之一例的基 本構成構件的側視圖。於設置於支持台2丨上之支柱22上, 安裝有端子部固定部25、光學偵測器固定部29。 以下’藉由圖7、圖8,說明高精度地測量微多孔膜之膜 厚t之方法。圖7係表示將微多孔膜放置於試料台23上之狀 123124.doc -13- 200831278 態的圖’圖8係表示將測量端子桿24載置於微多孔膜上之 狀態的圖。如圖7、圖8所示,將作為測量試料之微多孔膜 37載置於试料台23與測量端子桿24之間,使測量端子桿手 動上下指示桿25移動,從而由測量端子桿24與試料台23夾 持微多孔膜37,光學偵測部3〇利用來自例如承壓調整部固 定部32之反射光等,讀取與測量端子桿24直接聯結之承壓 調整部固定部32之上下動作,且將其換算成膜厚並讀取膜 厚。關於該光學偵測部之測量技術,例如,如keyenee& 司之綜合内部專用等之目錄中所介紹般,可使用共焦測量 方式、三角測距方式、自動對準方式、光波測距方式等方 式。於最佳之例中,理想的是使用三角測距方式之光學偵 測器。所謂三角測距方式係,使所投射之雷射光之對象物 的表面的擴散反射光之一部分聚光於受光透鏡處、並於 CCD(Charge c〇uPle device,電荷耦合器件)上成像的方 式’其中’當對象物移位時,擴散反射光之聚光角度移 位’ CCD上之成像位置移動,此時檢測該移動,將移動量 換算成與膜厚相對應之值,並讀取該移動量作為膜厚。較 好的是,此時所使用之光學偵測部3〇之分辨能為1 下’更好的是為〇 · 1 μϊη以下,進而更好的是0 〇 i 以下。 又’較好的是,由測量端子桿24與試料台23夾持微多孔膜 37後’經過特定時間,例如5秒〜1分鐘,較好的是5〜3〇秒 後再進行測量。作為較好之光學偵測器之具體例,可列舉 keyence公司製造之lk_G15。 為以良好的再現性及精度測量微多孔膜之厚度,重要的 123124.doc -14- 200831278 疋忒料台23與測量端子桿24平行。為此,較好的是如圖6 所不般δ又置測量端子平行度調整構件27,使得可進行微調 整。更好的是,利帛水平儀使試料台23表現出水平性後, 調正试料台與測量端子桿之平行度。對於測量端子桿之直 徑亚無特別限定,較好的是1〜20 mm,更好的是1〜1〇 mm圖6〜圖8之例巾,作為測量端子才旱,係使用直徑為$ mm者’且其垂直度已經過檢查。 進而,於藉由光學偵測部讀取測量端子桿之動作之情形 時車乂理想的是於恆溫室中測量膜厚,從而使得不會產生 曰間差。 又,為使用複數台測量裝置能夠以良妤的再現性及精度 而測里微多孔膜之厚度,較好的是使接觸微多孔膜之測量 輪子桿的承壓固定。圖6〜圖8之例中,於測量端子桿%之 類比顯不部26的上部設置有承壓調整部28 ,用以載置用來 對測量端子桿24進行承壓調整的砝碼,且將測量端子桿% 之承壓調整為固定,並藉由承壓調整部固定部U加以固 定圖6〜圖8之例中,為使得可藉由承壓調整部28調整測 里端子#24之承壓,而如圖7所示般,使用測量端子桿% 於類比顯示部26之内部形成為-體者。作為用以使測量端 =桿24之承壓為特定的其他方法,例如,亦可使複數台測 量裝置中所使用之測量端子桿自身之重量相同。 [聚烯烴製微多孔膜捲繞物之製造方法] 本發明之無捲繞鬆弛或過度之捲繞緊繃、外徑精度較高 之聚烯烴製微多孔膜捲繞物可藉由下述方式製造:對捲繞 123124.doc -15- 200831278 於母輥上之聚烯烴製微多孔膜,於其總寬度上將其切割成 特定寬度,之後,於將所切割出之各聚烯烴微多孔膜捲繞 於卷芯上時,分別對由聚烯烴製微多孔膜所構成之各捲繞 • 物的捲取張力進行控制。 Λ 分別對各捲繞物之捲取張力進行控制之方法並無限定。 例如,可藉由下述方式而分別對各捲繞物之捲取張力進行 、 控制,即,將所切割出之各聚烯烴微多孔膜,捲繞於分別 # 具有旋轉驅動部之單獨的卷芯上,利用各自之旋轉驅動部 使各卷芯旋轉,藉此來控制各捲繞物之捲取張力。又,若 係將所切割出之各聚稀烴微多孔膜捲繞於具有共用之旋轉 驅動部的卷芯、或固定在具有共用之旋轉驅動部之旋轉抽 上的複數個卷芯上之情形時,可利用其他方式分別對各聚 烯烴微多孔膜設置單獨之張力控制裝置,從而分別對各捲 繞物之捲取張力進行控制。 本發明之捲繞物尤其是可藉由下述方式而較好地獲得, # 即,使用單獨驅動式切割機切割聚烯烴製微多孔膜,並將 捲、%於言(卷心)上。由於單獨驅動式切割機於母輥總寬 度上進行切割時,可分別對各切割輥進行張力控制,故而 ’ 適於高效地製造本發明之聚烯烴製微多孔膜捲繞物。 •- 作為單獨驅動式切割機之例,有具有如圖4所示之複數 ' 個驅動傳达部6的切割機。驅動傳送部6使用有例如磁粉離 -器等與藉由共用之AC(alternating current,交流電)馬 達而運動之輥9相連結,設置於管夾頭部8之管(未圖示)的 捲取可藉由使得可藉由正時皮帶(timing bA)7等且由驅動 123l24.doc -16- 200831278 傳送部進行驅動而進行。於使用有磁粉離合器之情形時, 可利用電信號控制其輸出扭矩。因此,藉由針對各個單獨 之官捲取部進行張力檢測,並施加電性反饋,可對應於各 個單獨之管捲取部之張力進行捲繞。圖5中,表示有如此 之裝置之概略圖。自母輥π抽出之切割前之聚烯烴製微多 孔膜’被切割器14切割成所需之寬度,並捲繞於具有單獨 臂部13(各單獨之捲取部)且由共用之軸(未圖示)所支持之 管上。與此相對,當先前之同軸驅動型切割機於母親總寬 度上進行切割,並捲繞於具有共用之捲取部之管上時,係 配合相鄰之複數個捲繞物中之特定之捲繞物而進行張力控 制,故而所獲得之捲繞物會捲繞得較緊、或捲繞得較鬆, 因此較難對外徑進行控制,難以較好地獲得本發明之捲繞 物。又,亦容易產生捲繞偏移。 再者,本發明中之所謂單獨驅動式切割機,係切割並捲 繞網狀物之裝置,意指將切割後之各網狀物捲繞於各自具 有旋轉驅動部之單獨之卷芯上者。 捲取聚烯烴製微多孔膜時之捲取張力較好的是,使母輥 之抽取張力為125(N/m)以下左右,使各捲繞物之捲取張力 與抽取張力大致相等(較好的是±20%以内)。捲取張力之具 體值例如可以下述方式確定··使捲取張力於上述範圍内變 化並進行複數次捲繞,測量所獲得之捲繞物之捲繞鬆緊 度,並根據其結果進行確定。 本發明中,聚烯烴製微多孔膜捲繞物之鬆緊度較妤的 是’與卷怒相距5 mm處為34 N以下。當緊於該鬆緊度而捲 123124.doc -17- 200831278 繞時,會導致捲繞物之卷形狀不良。 又,較好的是,聚烯烴製微多孔膜捲繞之與卷芯相距1〇 mm處之鬆緊度(F(10))、及與卷芯相距20 mm處之鬆緊度 (F(20))的差(F(10)_F(20))為 0·05 N以上 2 N以下。若 F(10)-F(20)之值在該範圍内,則可減少捲繞偏移、錯位鬆脫等 不良。= The so-called "thickness t evaluated by the film" is:,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, The outermost microporous J' of the wound film of the porous film is measured at a plurality of positions at equal intervals in the width direction, and the average value of the nose is 9. In the present invention, the film of the microporous film made of a polysulfide is used. The thickness measurement method is limited, for example, in addition to the method shown in the following embodiments, it can also be measured with high precision by the method described below, that is, the measurement terminal is placed on the micro-film , read its action and convert it into film thickness. An optical detector can be used, for example, during the reading of the action of the measuring terminal. Further, it is preferred that the pressure per unit area carried by the microporous membrane is controlled within a fixed range by measuring the terminals. Further, it is preferred to perform measurement in a constant temperature chamber. Fig. 6 is a side view showing a basic constituent member of an example of a device for measuring the film thickness t of the microporous film. A terminal fixing portion 25 and an optical detector fixing portion 29 are attached to the pillar 22 provided on the support table 2A. Hereinafter, a method of measuring the film thickness t of the microporous film with high precision will be described with reference to Figs. 7 and 8 . Fig. 7 is a view showing a state in which the microporous film is placed on the sample stage 23. Fig. 8 is a view showing a state in which the measurement terminal rod 24 is placed on the microporous film. As shown in FIG. 7 and FIG. 8, the microporous film 37 as a measurement sample is placed between the sample stage 23 and the measurement terminal rod 24, and the measurement terminal rod is manually moved up and down the indicator rod 25, thereby measuring the terminal rod 24. The microporous film 37 is held by the sample stage 23, and the optical detecting unit 3 detects the pressure adjusting portion fixing portion 32 directly coupled to the measuring terminal rod 24 by using reflected light from the pressure adjusting portion fixing portion 32 or the like. Move up and down, convert it to a film thickness, and read the film thickness. Regarding the measurement technique of the optical detection unit, for example, as described in the catalogue of the key internals of the Keyenee & Division, the confocal measurement method, the triangulation method, the automatic alignment method, the optical wave ranging method, etc. can be used. the way. In the best case, an optical detector using a triangulation method is desirable. The triangulation method is a method in which a part of the diffused reflected light on the surface of the object of the projected laser light is condensed on the light receiving lens and imaged on a CCD (Charge c〇uPle device). Wherein 'when the object is displaced, the concentrating angle of the diffused reflected light shifts' the imaging position on the CCD moves, and at this time, the movement is detected, the amount of movement is converted into a value corresponding to the film thickness, and the amount of movement is read. As the film thickness. Preferably, the resolution of the optical detecting portion 3 used at this time is 1 ’, more preferably 〇 1 μϊη or less, and even more preferably 0 〇 i or less. Further, it is preferable that the microporous film 37 is sandwiched between the measuring terminal rod 24 and the sample stage 23, and the measurement is performed after a predetermined period of time, for example, 5 seconds to 1 minute, preferably 5 to 3 seconds. As a specific example of a preferable optical detector, lk_G15 manufactured by Keyence Corporation can be cited. In order to measure the thickness of the microporous film with good reproducibility and precision, it is important that the table 23 is parallel to the measuring terminal rod 24. For this reason, it is preferable to measure the terminal parallelism adjusting member 27 as shown in Fig. 6, so that fine adjustment can be performed. More preferably, after the level of the sample table 23 is leveled, the parallelism between the sample stage and the measuring terminal rod is adjusted. The diameter of the measuring terminal rod is not particularly limited, and is preferably 1 to 20 mm, more preferably 1 to 1 mm. The case of Fig. 6 to Fig. 8 is used as a measuring terminal, and the diameter is $ mm. 'and its verticality has been checked. Further, in the case where the operation of measuring the terminal rod is read by the optical detecting portion, it is desirable to measure the film thickness in the constant temperature chamber so that no coma is generated. Further, in order to measure the thickness of the microporous membrane with good reproducibility and precision using a plurality of measuring devices, it is preferable to fix the pressure of the measuring wheel rod contacting the microporous film. In the example of FIGS. 6 to 8, a pressure receiving portion 28 is provided on the upper portion of the analog display portion 26 such as the measuring terminal rod % for placing a weight for adjusting the pressure of the measuring terminal rod 24, and The pressure of the measuring terminal rod % is adjusted to be fixed, and is fixed by the pressure adjusting portion fixing portion U in the example of FIGS. 6 to 8 so that the pressure measuring portion 28 can be adjusted by the pressure adjusting portion 28. The pressure is applied, and as shown in Fig. 7, the measurement terminal rod % is formed as a body inside the analog display portion 26. As another method for making the measurement end = the pressure of the rod 24 specific, for example, the weights of the measurement terminal rods used in the plurality of measuring devices themselves may be the same. [Method for Producing Polyolefin Microporous Film Winding] The polyolefin microporous film winding of the present invention which has no winding slack or excessive winding tightness and high outer diameter precision can be obtained by the following means Manufacture: Pair of polypropylene microporous membranes wound on a mother roll, 123124.doc -15- 200831278, which are cut to a specific width over the entire width thereof, and then, the polyolefin microporous membranes to be cut out When wound around a winding core, the winding tension of each of the wound materials composed of the polyolefin microporous film is controlled.方法 The method of controlling the winding tension of each winding is not limited. For example, the winding tension of each of the wound materials can be controlled and controlled by winding each of the cut polyolefin microporous membranes into separate volumes having respective rotary driving portions. On the core, the winding cores are rotated by the respective rotation driving portions, thereby controlling the winding tension of each of the windings. Further, when the cut polysulfide microporous film is wound around a core having a common rotary drive portion or a plurality of cores fixed to a rotary pump having a common rotary drive portion In this case, a separate tension control device may be separately provided for each of the polyolefin microporous membranes to control the winding tension of each of the wound materials. The winding of the present invention can be preferably obtained, in particular, by cutting a polyolefin microporous film using a separate driven cutter and winding the roll on a core. Since the individual drive cutter can perform the tension control on each of the cutter rolls when the total width of the mother rolls is cut, it is suitable for efficiently producing the polyolefin microporous film wound of the present invention. • As an example of a single drive cutter, there is a cutter having a plurality of drive transmissions 6 as shown in FIG. The drive transmission unit 6 is connected to a roller 9 that is moved by a shared AC (alternating current) motor, for example, by a magnetic powder dispenser, and is wound around a tube (not shown) provided in the tube clamp head 8. This can be done by driving the timing bA 7 or the like and driving the drive 123l24.doc -16-200831278. In the case of a magnetic powder clutch, an electrical signal can be used to control its output torque. Therefore, by performing tension detection for each of the individual official winding portions and applying electrical feedback, the winding can be performed in accordance with the tension of each individual tube winding portion. Fig. 5 is a schematic view showing such a device. The polyolefin microporous film 'before cutting before being taken out from the mother roll π is cut into a desired width by the cutter 14, and wound around a single arm portion 13 (each separate winding portion) and shared by the shaft ( Not shown) on the supported tube. In contrast, when the prior coaxial drive type cutter cuts on the total width of the mother and winds on the tube having the shared take-up portion, it matches the specific volume of the adjacent plurality of windings. The tension control is performed around the object, so that the obtained wound material is wound tightly or loosely wound, so that it is difficult to control the outer diameter, and it is difficult to obtain the wound material of the present invention well. Moreover, the winding offset is also likely to occur. Furthermore, the so-called single drive cutter of the present invention is a device for cutting and winding a web, which means that the cut webs are wound on separate cores each having a rotary drive portion. . When the polyolefin microporous film is taken up, the take-up tension is preferably such that the take-up tension of the mother roll is about 125 (N/m) or less, so that the winding tension of each of the wounds is substantially equal to the take-up tension (Comparative) Good is within ±20%). The specific value of the take-up tension can be determined, for example, by changing the take-up tension within the above range and performing a plurality of windings, and measuring the winding tightness of the obtained wound product, and determining the result based on the result. In the present invention, the tightness of the polyolefin microporous film wound is less than 34 N at a distance of 5 mm from the roll anger. When wound around the tightness and the roll 123124.doc -17- 200831278, the winding shape of the winding is poor. Further, it is preferred that the polyolefin microporous film is wound at a distance of 1 mm from the core (F(10)) and at a distance of 20 mm from the core (F(20) The difference (F(10)_F(20)) is 0·05 N or more and 2 N or less. When the value of F(10)-F(20) is within this range, defects such as winding deviation and misalignment can be reduced.

此處,所謂捲繞物之鬆緊度,係用以評估捲繞物之捲繞 狀態的指標之一,意指將前端之直徑為〇·〇4〜〇·〇7 mm、針 尖角度為25〜27。、針尖R為〇·〇4〜〇·〇7 mm的針扎入捲繞物 之側面1 cm所需之力(N)。又,所謂相距卷芯之距離,意 指於捲繞物之側面,距離卷芯表面之與卷芯剖面(圓)之切 線相垂直之方向的距離。 捲、、物之緊度,例如可藉由依據《,1996 年I2月號之「切條機/捲取機簡單基礎技術講座第7講 捲取輥之品質中所介紹之「Smith •㈣緊度試驗機」的 下述方法而加以測量。 圖9表示用以測量捲繞物之鬆緊度之裝置的概略圖。捲 繞物之鬆緊度測量裝置1G1係將針安裝㈣力計上者。捲 繞物之鬆緊度可藉由下述方式進行測量:將測量裝置ι〇ι 之針的前端札入測量位置,並垂直下壓測量裝置101,直 至針插入i cm為止,測量此時之峰值荷重。作為如此之裝 置’例如’可使用切取Kokuyo製造之安全銷「gw之 if38麵.的針侧之後,安裝於日本計量^業⑽an """η Μ"" Μ6" C°.,Ltd.)(股)之數位測力計购〇上 123124.doc • 18 - 200831278 所得之裝置。 進而,當使用單獨驅動式切堂,丨4也丄 莉式切割機切割捲繞於母輥上之聚 細煙製微多孔膜,製造聚# ^ 多孔膜捲繞物時,於提 供可進一步降低電極•隔離膜一 騰體型捲繞物之插入外殼時 的插入不良的捲繞物之方面考詹 可慮,較好的是,使於母輥總 寬度上切割出之捲繞偏蒋兔S _ 褐移為5_以内的捲繞物群中,根據 下述式(1)所計算出之膜厚TQm、盥姻L u ^ 厅Ημιη)與對一片所評估出之膜厚Here, the tightness of the winding is one of the indexes for evaluating the winding state of the wound, meaning that the diameter of the front end is 〇·〇4~〇·〇7 mm, and the tip angle is 25~ 27. The needle tip R is the force (N) required for the needle to be inserted into the side of the winding 1 cm from 〇·〇4~〇·〇7 mm. Further, the distance from the winding core means the distance from the side surface of the winding body in the direction perpendicular to the tangential line of the winding core section (circle). The tightness of the volume and the object can be, for example, based on the "Smith • (4) tightly described in the quality of the winding roller of the "Scissor/Winding Machine Simple Basic Technology Lecture, I. The measurement method was measured by the following method. Fig. 9 is a schematic view showing an apparatus for measuring the tightness of a wound. The tightness measuring device 1G1 of the wound body is to mount the needle on the force meter. The tightness of the winding can be measured by taking the front end of the measuring device ι〇ι into the measuring position and pressing the measuring device 101 vertically until the needle is inserted into the icm, and the peak value is measured. Load. As such a device, for example, it is possible to use the needle side of the safety pin "gw's if38 face" manufactured by Kokuyo, and then install it in Japan's metering industry (10) an """η Μ""Μ6" C°. The digital dynamometer of Ltd.) is purchased from 123124.doc • 18 - 200831278. Further, when a separate drive type is used, the 丨4 is also cut and wound on the mother roll. In the case of producing a poly-porous microporous film, when a poly-[*] porous film winding is produced, it is possible to provide a winding material which can further reduce the insertion of the electrode/separator-type winding body into the outer casing. It is preferable that the film is calculated according to the following formula (1) in a group of windings in which the winding of the mother roll S__ is browned to within 5_ of the total width of the mother roll. Thick TQm, 盥 marriage L u ^ Ημιη) and the thickness of the film evaluated

Κμηι)之差(膜厚差)的標準偏差 干爾產為0·7 μπι以下,更好為〇·5 jim以下, T(pm)=7c(D2_d2)/4L ⑴ (上述式(1)中’ D係指捲繞於卷芯上之包含多孔膜之捲繞 物的外徑(叫’⑽指卷芯之外徑卜),以指捲繞物之 卷長(m))。 於本發明中,就捲繞性、成本方面考慮,用以捲繞聚烯 烴製微多孔膜之卷芯尺寸較好的是,其外徑為9ι·8瓜㈤以 上。所使用之卷芯,通常係根據内徑而稱呼。外徑為91·8 mm之紙管通常内徑為76·2 mm,紙厚為5〜15㈤瓜之範圍, 可根據強度而調整。作為所使用之管,可使用通常市售之 公差為±0.5 mm且更好的是±〇·3 mm之紙管、或塑料管,較 好的是公差較小者。 本發明之捲繞物將發揮可提供一種可減少插入外殼時之 插入不良的電極•隔離膜體型捲繞物的效果,並且,於作 為使用有寬度較寬之隔離膜(例如6〇〜160 mm)、卷長較長 之隔離膜(例如500〜3000 m,較好的是800〜2500 m)的電 123124.doc -19- 200831278 極•隔離膜捲繞物而使用之情形時,上述效果特別明顯。 若使用本發明之聚烯烴製微多孔膜捲繞物,則可提供一 種如下所述之電極·隔離膜捲繞物,即,於將聚烯烴製微 多孔膜捲繞於卷芯上之捲繞物中,可明確出捲繞於卷芯上 之包含多孔膜之捲繞物的外徑以及根據卷芯之外徑及卷長 而計算出的膜厚(μηι),從而可減少插入外殼時之插入不 良。 [聚烯烴製微多孔膜] 本發明之聚烯烴製微多孔膜之孔徑較好的是 μηι,更好的是〇·〇ι〜〇·ι μιη。本發明中,微多孔膜之孔徑 Γ(μπι)如下所述:悉知毛細管内部之流體於流體之平均自 由路徑大於毛細管之孔徑時按照努生流動(Knudsen flow),而當小於毛細管之孔徑時按照普塞流動(p〇iseuille flow) ’利用該點’將微多孔膜之透氣度測量中之空氣流動 假定為努生流動’又’將微多孔膜之透水度測量中之水流 動假定為普塞流動,並藉由下述式加以表示: r=2vx(Rliq/Rgas)x(16n/3Ps)x 106。 此處,Rgas為空氣之透過速度常數(m3/(m2.sec.pa)), Rliq為水之透過速度常數(m3/(m2,sec*Pa)),v為空氣之分 子速度(m/sec) ’ η為水之黏度(Pa*sec)(=0.8950 mPa.sec at 25°C),Ps為標準壓力(Pa)(=101325 Pa),其等分別可以下 述式表示:标准μηι) The standard deviation of the difference (film thickness difference) is 0. 7 μπι or less, more preferably 〇·5 jim or less, T(pm)=7c(D2_d2)/4L (1) (in the above formula (1) 'D' refers to the outer diameter of the wound containing the porous film wound on the core (referred to as '(10) means the outer diameter of the core) to mean the length (m) of the wound. In the present invention, the winding core for winding the polyolefin microporous film preferably has an outer diameter of 9 · 8 or more (five) or more in terms of winding property and cost. The core used is usually referred to by the inner diameter. A paper tube having an outer diameter of 91·8 mm usually has an inner diameter of 76·2 mm and a paper thickness of 5 to 15 (five), which can be adjusted according to the strength. As the tube to be used, a commercially available paper tube having a tolerance of ±0.5 mm and more preferably ±〇·3 mm, or a plastic tube can be used, and it is preferable that the tolerance is smaller. The winding of the present invention will exert an effect of providing an electrode/separator-type winding wound which can reduce insertion failure when inserted into a casing, and can be used as a separator having a wide width (for example, 6 〇 to 160 mm). ), the film with a long coil length (for example, 500 to 3000 m, preferably 800 to 2500 m) of electricity 123124.doc -19- 200831278 pole • when the separator is wound and used, the above effect is special obvious. When the polyolefin microporous film wound of the present invention is used, it is possible to provide an electrode/separator winding as described below, that is, a winding for winding a polyolefin microporous film on a winding core. The outer diameter of the wound material including the porous film wound around the winding core and the film thickness (μηι) calculated from the outer diameter and the coil length of the winding core can be clarified, thereby reducing the time when the outer casing is inserted. Poor insertion. [Polyolefin-made microporous film] The polyolefin microporous film of the present invention preferably has a pore diameter of μηι, more preferably 〇·〇ι~〇·ι μιη. In the present invention, the pore diameter Γ(μπι) of the microporous membrane is as follows: it is known that the fluid inside the capillary is in a Knudsen flow when the average free path of the fluid is larger than the pore diameter of the capillary, and is smaller than the pore diameter of the capillary. According to the p〇iseuille flow 'use this point', the air flow in the gas permeability measurement of the microporous membrane is assumed to be a normal flow 'and' the water flow in the permeability measurement of the microporous membrane is assumed to be The plug flows and is represented by the following formula: r = 2vx (Rliq / Rgas) x (16n / 3Ps) x 106. Here, Rgas is the air transmission velocity constant (m3/(m2.sec.pa)), Rliq is the water transmission velocity constant (m3/(m2, sec*Pa)), and v is the molecular velocity of air (m/ Sec) 'η is the viscosity of water (Pa*sec) (=0.8950 mPa.sec at 25°C), and Ps is the standard pressure (Pa) (=101325 Pa), which can be expressed by the following formula:

Rgas=0.0001/(透氣度 χ(6·424χ10-4)χ(0·01276χ 101325))。 再者,透氣度係依據JISP-8117而求出: 123124.doc -20- 200831278Rgas=0.0001/(Air permeability χ(6·424χ10-4)χ(0·01276χ 101325)). Furthermore, the air permeability is determined according to JISP-8117: 123124.doc -20- 200831278

Rliq=透水度/100。 再者,透水度可以如下所述之方式求出。將預先浸潰於 乙醇中之微多孔膜設置於直徑41 mm的不錄鋼製透液單元 . 中,以水清洗該膜之乙醇後,以約50000 Pa之壓差使水透 過’根據經過120似時之透水量(Cn^,計算出單位時間· 單位壓力•單位面積之透水量,並以此作為透水度: ‘ ν=((8ΙΙχΤ)/(πχΜ))1/2。 Φ 再者,R為氣體常數(=8·314),Τ為絕對溫度(κ),π為圓 周率,Μ為空氣之平均分子量卜 聚烯烴製微多孔膜之空隙率較好的是25%以上75%以 下。此處,空隙率(。/。)可以由下述式表示: 空隙率(%)=[{V-(M/p)}/V]xl〇〇。 式中,v為微多孔膜之體積(cm3),M為微多孔膜之質量 (g) ’ P為構成微多孔膜之樹脂或樹脂組合物的密度 (g/cm3) 〇 • 具體而言,例如可藉由下述方式計算出:自微多孔膜切 取10 cmxl〇 cm見方之試料,求出其體積(cm)及質量(§), 根據該體積(cm)及質量(g)、以及構成膜之聚烯烴樹脂組合 物之禮度(g/cm3),藉由上式而計算出空隙率。再者,本發 ‘ ’ 明中’於微多孔膜包含聚乙烯之情形時,設聚乙烯之密度 為〇_95而進行計算。又,聚烯烴製微多孔膜之膜厚t較好的 是3 μχη以上2〇〇 μχη以下。 聚婦烴製微多孔膜之TD方向之動摩擦係數較好的是〇 . 6 以下,更好的是〇·1〜〇·4。TD方向之動摩擦係數例如可以 123124.doc -21 - 200831278 下述方式測量:對寬度50 mmx測量方向200 mm之試料, 使用Kato Tech股份有限公司製造iKES-S]E摩擦試驗機, 並於荷重50 g、接點面積1〇xl〇=1〇〇 mm2(纏繞有2〇根〇·5 _ 之琴鋼絲)、接點傳送速度1 mm/sec、張力6 kPa、温 度25°C之條件下進行測量。再者,由於TD方向之動摩擦係 數為0.1〜0.4之聚烯烴製微多孔膜容易產生捲繞偏移等不 • 良’故而尤其好的是使用本發明之捲繞物之製造方法進行 捲繞。 又’於捲入有異物之情形時,於過度緊繃捲繞之捲繞物 中’微多孔膜容易被損壞,當用作電池用隔離膜時,介電 強度不良品之比例將會增加。該傾向尤其會於僅實施有轴 延伸之縱橫向之拉伸強度相差10倍以上的高異向性微多孔 膜中顯著產生。 因此,本發明之無捲繞緊繃之棬繞物及其製造方法特別 適用於使用縱方向之拉伸強度(MD拉伸強度)與寬度方向之 φ 拉伸強度(10拉伸強度)之比(MD拉伸強度/TD拉伸強度)為 10以上者作為聚烯烴製微多孔膜的情形。 本發明中所使用之聚烯烴製微多孔膜,例如可藉由下述 - 方式製作。 作為聚烯烴,可使用聚烯烴單獨物以及2種以上之聚烯 - 烴混合物。作為主成分之聚烯烴,例如可列舉聚乙浠、聚 丙烯、聚-4-甲基戊烯等。作為主成分以外之聚烯烴, 可於不損及製膜性,且不損害本發明之目的的範圍内,調 配各種聚烯烴。例如,可調配用以提昇孔阻塞特性的心烯 123124.doc -22- 200831278 煙共單體的含量較高之低溶點聚乙烯、或用以提昇耐熱性 之聚丙烯以及聚-4-甲基-1-戊烯等。又,亦可於不損室作 為電池用隔離膜之性能、不損害製膜性、並且不損宝本發 明之目的的範圍内,調配聚烯烴以外之聚合物材料或其他 有機及無機材料。於構成微多孔膜之聚烯烴組合物中,視 需要,可混合使用酚系、磷系、疏系等之抗氧化劑,硬脂 酸鈣、硬脂酸辞等金屬皂類,紫外線吸收劑,光穩定劑, 抗靜電劑,防霧劑,染色顏料等公知之添加劑。 本發明之聚烯烴製微多孔膜之製造方法並無特別限制, 可採用所謂之乾式法、濕式法等。作為利用所謂濕式法之 製造方法,例如,可藉由下述方式製作聚烯烴製徼多孔 膜,將上述聚烯烴,於其熔點以上之溫度溶解於稱作可塑 劑之〉谷劑中,將所獲得之溶液冷卻至結晶溫度以下為止, 生成南分子凝膠,使用該高分子凝膠進行成膜(成膜步 驟),延伸所獲得之膜(延伸步驟),之後,去除可塑劑 塑劑去除步驟)。 此處所。之可塑劑,意指於其沸點以下之溫度可與聚烯 烴形成均一之溶液的有機化合物,作為其具體例,可列舉 十氫奈、一甲苯、鄰苯二甲酸二辛酯、鄰苯二曱酸二丁 酯、十八烷醇、油醇、癸醇、壬醇、二苯醚、正癸烷、正 十二烷、石蠟油等。又,亦可使用自可塑劑去除步驟再生 之可塑劑。 對分子凝膠中之可㈣之比例並無特別限定,較好的是 20重量%〜9〇重量%,更好的是5〇重量%〜8〇重量%。若可塑 123124.doc -23- 200831278 劑之比例為20重量%以下,則存在難以獲得具有適當之空 隙率之微多孔膜的傾向;若為9〇重量%以上,則熱:液: 黏度降低’存在片材難以連續成形之傾向。 . 以下,將聚烯烴製微多孔膜之製造方法之一例劃分為上 述製膜步驟、延伸步驟以及可塑劑去除步驟加以說=。 ' [成膜步驟] 成膜方法並無特別限定,例如,藉由下述方式,即,將 響 混合聚烯烴粉末及可塑劑供給於擠出機中,於2〇(rc左右 之溫度將兩者熔融混練後’自通常之衣架模(加^㈣ die)澆鑄至冷卻輥上,可連續形成膜厚為幾十奈米至幾毫 米之片封。 、 [延伸步驟] 繼而,將所獲得之片材沿至少單軸方向延伸,藉此形成 延伸膜。延伸方法並無特別限定,可使用拉幅法、親法、 壓延法等。其中,較好的是利用拉幅法之同時進行雙轴延 • 伸。延伸溫度可為自常溫至高分子凝膠之熔點為止之溫 度,較好的是80〜140°C,更好的*1〇〇〜13〇t:。延伸倍率 較好的是,面積倍率為4〜400倍,更好的是8〜2〇〇倍更好 • 的是16〜100倍。若延伸倍率為4倍以下,則作為隔離膜之 … 強度不充分,若為4〇〇倍以上,則存在不僅難以延伸而且 • 谷易導致所獲得之微多孔膜之空隙率較低等弊端的傾向。 [可塑劑去徐步驟] 繼而,自延伸膜去除可塑劑,藉此可獲得微多孔膜。可 塑劑之去除方法並無特別限定。例如,於使用石蠟油或鄰 123124.doc -24 - 200831278 苯二甲酸二辛酯作為可塑劑之情形時,可以利用二氯甲俨 或甲基乙基酮等有機溶劑將其等萃取出,但亦可藉由對= 獲得之微多孔μ ’於其熔點溫度以下之溫度進行過熱乾 燥,而充分去除。又,例如於使用十氫萘等低彿點化:: 作為可塑劑之情形時,僅於微多孔膜之熔點溫度以下之溫 度進行加熱乾燥即可將其去除1實現低成本,可回收使 用後之有機溶劑並再次用於去除可塑劑。為改善透過性,Rliq = water permeability / 100. Further, the water permeability can be obtained as follows. The microporous membrane preliminarily impregnated in ethanol is placed in a non-recorded steel liquid permeable unit having a diameter of 41 mm. After washing the ethanol of the membrane with water, the water is passed through a pressure difference of about 50,000 Pa. The amount of water permeation (Cn^, calculate the unit time, unit pressure, per unit area of water permeability, and use this as the water permeability: ' ν = ((8 ΙΙχΤ) / (π χΜ)) 1/2. Φ Again, R is a gas constant (=8·314), Τ is an absolute temperature (κ), π is a pi, and Μ is an average molecular weight of air. The porosity of the polyolefin microporous film is preferably 25% or more and 75% or less. Here, the void ratio (./.) can be expressed by the following formula: void ratio (%) = [{V - (M / p)} / V] xl 〇〇 where v is the volume of the microporous membrane (cm3), M is the mass of the microporous membrane (g) 'P is the density (g/cm3) of the resin or resin composition constituting the microporous membrane. Specifically, for example, it can be calculated by the following method: A sample of 10 cm×l〇cm square was cut out from the microporous membrane to determine the volume (cm) and mass (§), based on the volume (cm) and mass (g), and the polyolefin constituting the membrane. The viscosity of the fat composition (g/cm3) is calculated by the above formula. Further, in the case where the microporous film contains polyethylene, the density of the polyethylene is 〇. Further, the film thickness t of the polyolefin microporous film is preferably 3 μχη or more and 2 μμχη or less. The directional friction coefficient of the polystyrene-made microporous film in the TD direction is preferably 〇. 6 Below, more preferably 〇·1~〇·4. The dynamic friction coefficient in the TD direction can be measured, for example, 123124.doc -21 - 200831278. For the sample with a width of 50 mmx and a measurement direction of 200 mm, use Kato Tech Limited The company manufactures iKES-S]E friction testing machine with a load of 50 g and a contact area of 1〇xl〇=1〇〇mm2 (wound wire with 2〇〇·5 _) and a joint transmission speed of 1 mm. The measurement is carried out under the conditions of /sec, the tension of 6 kPa, and the temperature of 25 ° C. Further, the polyolefin microporous film having a dynamic friction coefficient of 0.1 to 0.4 in the TD direction is liable to cause a winding offset or the like. Preferably, the winding method of the winding material of the present invention is used for winding. In the case of the object, the microporous film is easily damaged in the winding which is excessively tightly wound, and when used as a separator for a battery, the proportion of defective dielectric strength will increase. This tendency is particularly The high anisotropy microporous film having a tensile strength in the longitudinal direction and the transverse direction of the axial extension is significantly more than 10 times. Therefore, the winding-free tight wrap of the present invention and the method for producing the same are particularly suitable for use in the longitudinal direction. The ratio of the tensile strength (MD tensile strength) in the direction to the φ tensile strength (10 tensile strength) in the width direction (MD tensile strength/TD tensile strength) is 10 or more as a polyolefin microporous film. situation. The polyolefin microporous film used in the present invention can be produced, for example, by the following method. As the polyolefin, a polyolefin alone and two or more kinds of polyolefin-hydrocarbon mixtures can be used. Examples of the polyolefin which is a main component include polyacetonitrile, polypropylene, poly-4-methylpentene and the like. The polyolefin other than the main component can be blended with various polyolefins within a range that does not impair the film forming property and does not impair the object of the present invention. For example, it can be adjusted to improve the pore blocking characteristics of the heart. 123124.doc -22- 200831278 Low-melting point polyethylene with higher content of smoke comonomer, or polypropylene for improving heat resistance and poly-4-A Base-1-pentene and the like. Further, a polymer material other than polyolefin or other organic and inorganic materials may be blended in a range which does not impair the performance of the battery separator, does not impair the film forming property, and does not impair the purpose of the invention. In the polyolefin composition constituting the microporous film, if necessary, an antioxidant such as a phenol type, a phosphorus type or a drip system, a metal soap such as calcium stearate or stearic acid, or an ultraviolet absorber or a light absorber may be used. Known additives such as stabilizers, antistatic agents, antifogging agents, dyeing pigments, and the like. The method for producing the polyolefin microporous film of the present invention is not particularly limited, and a so-called dry method, wet method or the like can be employed. As a manufacturing method by the so-called wet method, for example, a polyolefin-made porous film can be produced by dissolving the above-mentioned polyolefin at a temperature equal to or higher than the melting point in a granule called a plasticizer. The obtained solution is cooled to a temperature lower than the crystallization temperature to form a south molecular gel, and the polymer gel is used for film formation (film formation step), and the obtained film is stretched (extension step), after which the plasticizer removal is removed. step). Here. The plasticizer means an organic compound which can form a uniform solution with a polyolefin at a temperature below its boiling point, and specific examples thereof include decahydronaphthalene, monomethylbenzene, dioctyl phthalate, and phthalic acid. Dibutyl acrylate, stearyl alcohol, oleyl alcohol, decyl alcohol, decyl alcohol, diphenyl ether, n-decane, n-dodecane, paraffin oil, and the like. Further, a plasticizer which is regenerated from the step of removing the plasticizer may also be used. The ratio of the (4) in the molecular gel is not particularly limited, and is preferably from 20% by weight to 9% by weight, more preferably from 5% by weight to 8% by weight. If the ratio of the plastic 123124.doc -23-200831278 agent is 20% by weight or less, there is a tendency that it is difficult to obtain a microporous film having an appropriate void ratio; if it is 9% by weight or more, the heat: liquid: viscosity is lowered' There is a tendency that the sheet is difficult to continuously form. Hereinafter, an example of a method for producing a polyolefin microporous film is divided into the above-described film forming step, stretching step, and plasticizer removing step. '[Film Forming Step] The film forming method is not particularly limited. For example, the ring-mixed polyolefin powder and the plasticizer are supplied to the extruder at a temperature of about 2 rc. After melt-kneading, 'the usual hanger mold (plus ^4) die is cast onto the cooling roll, and the film seal having a film thickness of several tens of nanometers to several millimeters can be continuously formed. [Extension step] Then, the obtained The sheet is stretched in at least a uniaxial direction to form a stretched film. The stretching method is not particularly limited, and a tenter method, a parent method, a calendering method, etc. may be used. Among them, it is preferred to carry out the two-axis method by the tenter method. The elongation temperature may be from the normal temperature to the melting point of the polymer gel, preferably 80 to 140 ° C, more preferably *1 〇〇 to 13 〇 t: the stretching ratio is better, The area magnification is 4 to 400 times, more preferably 8 to 2 times better. It is 16 to 100 times. If the stretching ratio is 4 times or less, it is used as a separator... The strength is not sufficient, if it is 4〇 If it is more than 〇, there is a microporous film that is not only difficult to extend but also The tendency of the void ratio is low, etc. [Plasticizer removal step] Then, the plasticizer is removed from the stretched film, whereby the microporous film can be obtained. The method of removing the plasticizer is not particularly limited. For example, using paraffin oil or邻123124.doc -24 - 200831278 When dioctyl phthalate is used as a plasticizer, it can be extracted by using an organic solvent such as dichloromethane or methyl ethyl ketone, but it can also be obtained by The microporous μ' is subjected to superheat drying at a temperature below its melting point temperature, and is sufficiently removed. Further, for example, low fossilization using decahydronaphthalene or the like: as a plasticizer, only the melting temperature of the microporous membrane The following temperatures can be removed by heating and drying to achieve low cost, and the used organic solvent can be recovered and reused for removing the plasticizer. To improve the permeability,

提高尺寸穩定性,下述方式亦較好,,對於藉由上述製 造方法而獲得之聚烯烴製微多孔膜,視需要而於熔點溫度 以下之溫度實施熱處理。 實施例 以下,藉由實施例以及比較例具體地說明本發明,該等 實施例以及比較例並不限制本發明之範圍。本發明中所使 用之各種物性,係根據以下之試驗方法而測量出。 (1)對一片所評估出之膜厚砍卜叫 自所切割出之微多孔膜切出25 cm之膜,使用東洋精機 製造之微測厚器(KBM型)於室溫23°C對10處進行測量,將 其平均值作為t。 ; (2)根據包含多孔膜之捲繞於管上之捲繞物之外握及卷 芯之外徑以及卷長而計算出之膜厚 使用日本專利特開2__88255號公報巾所記載之外徑測 量裝置’對切割並捲繞於已預先測量出外徑之卷芯咖⑷ 上的包含聚烯烴製微多孔膜的外徑D(mm)進行測量。若設 捲繞卷長為L(m),則可藉由下式 123124.doc -25- 200831278It is also preferable to increase the dimensional stability, and the polyolefin microporous film obtained by the above-described production method is subjected to heat treatment at a temperature equal to or lower than the melting point temperature as necessary. EXAMPLES Hereinafter, the present invention will be specifically described by way of Examples and Comparative Examples, which are not intended to limit the scope of the invention. The various physical properties used in the present invention were measured in accordance with the following test methods. (1) A film thickness of 25 cm was measured from a microporous membrane that was cut out, and a micro-thickness device (KBM type) manufactured by Toyo Seiki was used at room temperature of 23 ° C for 10 The measurement is performed, and the average value is taken as t. (2) The film thickness calculated from the outer diameter of the grip and the winding core of the porous film and the winding length of the wound core, and the outer diameter described in Japanese Patent Laid-Open Publication No. Hei 2__88255 The measuring device 'measured the outer diameter D (mm) of the microporous film containing polyolefin which was cut and wound on the core coffee (4) having the outer diameter measured in advance. If the winding length is L(m), it can be obtained by the following formula 123124.doc -25- 200831278

T(Hm)=7C(D2_d2)/4L 而求出T。 製微多孔膜之外徑D之測量 而於寬度方向上以1 mm為單 包S切割並捲繞之聚烯烴製微多 中,為了避開兩端之凸出部,而於寬 位而測里自兩端靠近内側3 mm之部分的外徑,並將其平均 值作為D。 (3)電極·隔離膜捲繞物之製作 、正極之製作··將92 2重量%之鋰鈷複合氧化物Lic〇〇2作 為活〖生物貝、分別為2·3重量%之鱗片狀石墨及乙炔黑作為 一電^、以及3·2重量%之聚偏二氟乙烯(PVDF)作為黏合 劑,分散於N-曱基吼略烧酮(NMp)中,製備出聚料。使用 杈塗佈機,將該漿料塗附於作為正極集電體之厚度為2〇 冶的單面上,於13〇〇乾燥3分鐘後,藉由輥壓機壤 縮成形。此時,使正極之活性物質塗附量為25〇 g/m2,活 陳物貝總體您、度為3 G() g/em3。將其切割成寬度約職, 形成帶狀。 負極之製作:將96·9重量%之人造石墨作為活性物質、 1,4重里/°之羧甲基纖維素之銨鹽及1.7重量%苯乙烯-丁二 烯共聚物礼膠作為黏合劑,分散於純水巾,製備出浆料。 使用模塗佈機,將該漿料塗附於作為負極集電體之厚度為 12 μιη之銅箔的單面上,於12〇它乾燥3分鐘後,藉由輥T is determined by T(Hm)=7C(D2_d2)/4L. The measurement of the outer diameter D of the microporous membrane is carried out in a polyolefin-made micro-multiple in which the width is 1 mm in a single-pack S-cut and wound, and is measured in a wide position in order to avoid the projections at both ends. The outer diameter of the portion 3 mm from the inner side from the both ends, and the average value is taken as D. (3) Preparation of Electrode/Separator Winding and Preparation of Positive Electrode··92 2% by weight of lithium cobalt composite oxide Lic〇〇2 as scalloped graphite of biobe, respectively, 2.3% by weight And acetylene black as a binder, and 3.2% by weight of polyvinylidene fluoride (PVDF) as a binder, dispersed in N-mercaptopurine (NMp) to prepare a polymer. This slurry was applied to a single surface having a thickness of 2 Å as a positive electrode current collector using a ruthenium coater, dried at 13 Torr for 3 minutes, and then formed by a roller press. At this time, the active material coating amount of the positive electrode is 25 〇 g/m 2 , and the total amount of the living animal is 3 G () g / em 3 . It is cut into widths to form a band. Preparation of the negative electrode: 96.9% by weight of artificial graphite as an active material, 1,4% by weight of ammonium salt of carboxymethylcellulose and 1.7% by weight of styrene-butadiene copolymer gum as a binder, Disperse in a pure water towel to prepare a slurry. Using a die coater, the slurry was applied to one side of a copper foil having a thickness of 12 μm as a negative electrode collector, and dried at 12 Torr for 3 minutes, and then passed through a roll.

Uk m b 相y 支Uk m b phase y branch

123124.doc :/,貝里附!钩ιυο g/m2, 。將其切割成寬度約 -26- 200831278 電極•隔離膜捲繞物製作:將上述微多孔膜隔離媒、帶 狀正極以及帶狀負極’以帶狀負極、隔離膜、帶狀正極、 . 隔離膜之順序重疊並捲繞複數圈形成漩渦狀,藉此,製作 • 出電極•隔離膜捲繞物。 " (4) 電極*隔離膜捲繞物之外殼插入性 使用以夾頭夾持所製作之捲繞物,並藉由外殼插入機自 . 動將其插入所準備之18 ππηφ之外殼中,評估上述捲繞 物。 攀 設外殼插入不良 100卷中〇卷以下最佳 2卷以下 良好 除此以外 不佳。 (5) 黏度平均分子量Μν 根據ASTM-D4020,求出實施例、比較例中所使用之聚 乙烯於十氫萘溶劑中之135°C時的極限黏度[η],並藉由下 述式計算出黏度平均分子量Μν。 φ [η]=6·77χΐ〇-1(Τ4Μν。·67 (6) 捲繞物之鬆緊度 切取Kokuyo製之安全銷「hin-Ι3」之總長38 mm的針 • 側,安裝於日本計量器工業(股)之數位測力計HF-10上, ” · 形成測量裝置。將其礼入捲繞物之側面,並垂直下按,直 至針插入1 cm為止,測量出峰值荷重。再者,Kokuyo製造 之安全銷「hin· 13」總長3 8 mm之針側的尖端形狀如下所 述··針尖角度為26。,針尖R為0.04〜0.07 mm,針尖剖面直 後為 〇·〇47 mm。 123124.doc -27- 200831278 (7) 透氣度(sec/100 cc) 依據JIS P-8117,使用Gurley式透氣度計(東洋精器(股) 製,G-B2(商標))進行測量。 (8) (MD拉伸強度/TD拉伸強度)此 依據JIS K7127,使用島津製作所製造之拉伸試驗機123124.doc :/, Berry attached! Hook ιυο g/m2, . Cut it into a width of about -26-200831278 electrode • separator winding preparation: the above microporous membrane separator, strip positive electrode and strip negative electrode 'with ribbon negative electrode, separator, ribbon positive electrode, . The order is superimposed and wound in a plurality of turns to form a spiral shape, thereby producing an electrode/spacer winding. " (4) Electrode* The outer casing of the separator winding is inserted and clamped by the chuck, and inserted into the prepared 18 ππηφ casing by the casing inserter. The above windings were evaluated. Climbing the casing is poorly inserted. The best volume under the 100-volume roll is below 2 rolls. Good Others Not good. (5) Viscosity average molecular weight Μν The ultimate viscosity [η] at 135 ° C of the polyethylene used in the examples and the comparative examples in the decalin solvent was determined according to ASTM-D4020, and was calculated by the following formula. The viscosity average molecular weight Μν. φ [η]=6·77χΐ〇-1 (Τ4Μν··67 (6) The tightness of the wound material is cut from the needle side of the safety pin "hin-Ι3" made by Kokuyo, 38 mm, and mounted on a Japanese meter. Industrial (unit) digital dynamometer HF-10, ” · Form the measuring device. Put it into the side of the winding and press it vertically until the needle is inserted 1 cm, and measure the peak load. Kokuyo's safety pin "hin·13" has a tip end shape of 3 8 mm on the needle side. The tip angle is 26. The tip R is 0.04 to 0.07 mm, and the tip of the needle is straight and then 〇·〇 47 mm. 123124 .doc -27- 200831278 (7) Air permeability (sec/100 cc) Measured according to JIS P-8117 using a Gurley type gas permeability meter (Toyo Seiki Co., Ltd., G-B2 (trademark)). (MD tensile strength / TD tensile strength) This is a tensile testing machine manufactured by Shimadzu Corporation according to JIS K7127.

Auto Graph AG-A型(商標),测f 执伸強度測量用樣品 以及TD拉伸強度測量用樣品(形狀·寬10 mmx長100 mm) 的拉伸強度。使用夾頭間距離為5〇 mm ’且於樣品兩端部 (各為 25 mm 寬)之單面上貼有 ce!1〇phane tape(Nitto Denko Corporation(股)製,商品名:N·29)者進而’為防止试驗 時樣品滑動,而將厚度為1 之氣橡膠勘貼於拉伸試驗機 之夾頭内侧。 以試驗前之樣品剖面積除樣品斷裂時所賦予之拉力,藉 此求出拉伸強度(MPa),計算出MD拉伸強度與TD拉伸強 度之值的比。再者,測量係於溫度23±2°C、夾頭壓0.30 MPa、拉伸速度200 mm/min(若為無法將夾頭間距離確保 為50 mm之樣品,則變形速度為400%/min)之條件下進行。 [實施例1] [聚烯烴製微多孔膜之製作] 使用輥攪拌機,將35重量%iMv為27萬之聚乙烯、與65 重量%之Mv為95萬之聚乙烯的混合物乾混和,從而獲得聚 烯烴組合物。藉由雙軸擠出機,對所獲得之30重量%之組 合物及7 0重量%之液體石壤進行均一之熔融混練,獲得聚 乙烯熔融混練物。熔融混練條件如下,設定溫度為 123124.doc -28 - 200831278 200 C、螺桿轉數為170 rpm、噴出量為15 kg/hr。繼而, 對熔融混練物使用保持於22(rCiT塑模(寬度為25〇 mm), 將溶融混練物擠出成片狀。 使用表面溫度控制為60°c之金屬輥對熔融混練物進行壓 著’並使其冷卻,藉此,獲得厚度為1〇〇〇 μχη之厚度穩定 性優異之凝膠片材。 繼而’使用同時雙轴延伸機,於延伸溫度125。〇延伸至 7x7倍’繼而’導入至甲基乙基酮槽中,於甲基乙基酮中 充为次潰,萃取去除液體石蠟,其後,乾燥去除甲基乙基 酮。 進面’使用拉幅延伸機,沿橫方向於〗2〇。〇延伸1 ·5倍, 於125°C進行熱固定,獲得橫向寬度為12 m、膜厚為18 μιη、空隙率為40%、孔徑為〇·〇5 μιη的微多孔膜。又,微 多孔膜之TD方向之動摩擦係數為〇.4。 [聚烯烴製微多孔膜捲繞物之製作] 為了使得當將細切成複數條之聚浠烴製微多孔膜捲取於 複數根卷芯上時能夠分別進行張力控制,而於各單獨之捲 取《卩中δΧ置張力檢測器,藉此,可分別檢測各細切之聚浠 烴製微多孔膜之張力’並根據該檢測值,控制各驅動源之 輸出扭矩。 使用單獨驅動切條機,將所製作之聚烯烴製微多孔膜切 割成寬60 mm,並捲繞於紙製管(尺寸等:3Β)上,獲得聚 烯烴製微多孔膜捲繞物。d、L分別為102 mm、1000 m。 切割8根母輥,製造出ι60卷聚烯烴製微多孔膜捲繞物, 123124.doc -29- 200831278 。自其中抽取 ,測量並計算 T 為 17.6 〜18·1 產生5 mm以上之捲繞偏移之捲繞物僅有1卷 150卷之捲繞偏移為5 mm以内之捲繞切割物 D、T、1 ’其結果為·· D為 181.2〜182.9 mm, μπι,|T_t|之最大值為1·2μιη,標準偏差為 F(5)之平均值為25 N,F(10)_F(2〇)i平均值 μπι、t為 17〜19 0·4 μπι 〇 又, 為1 Ν。 再者,相對於母輥之總寬度^ m’設切條機之抽取張Auto Graph AG-A (trademark), measured the tensile strength of the sample for tensile strength measurement and the sample for TD tensile strength measurement (shape, width 10 mm x length 100 mm). Use a ce!1〇phane tape (manufactured by Nitto Denko Corporation, trade name: N·29) with a distance between the chucks of 5〇mm' and on both sides of the sample (25 mm each) In order to prevent the sample from slipping during the test, a gas of a thickness of 1 is applied to the inside of the chuck of the tensile tester. The tensile strength (MPa) was determined by dividing the cross-sectional area of the sample before the test, and the ratio of the tensile strength of the MD to the value of the tensile strength of the TD was calculated. Furthermore, the measurement is performed at a temperature of 23 ± 2 ° C, a chuck pressure of 0.30 MPa, and a tensile speed of 200 mm / min (if it is impossible to ensure a distance of 50 mm between the chucks, the deformation speed is 400% / min) Under the conditions of ). [Example 1] [Production of polyolefin microporous film] A mixture of 35 wt% iMv of 270,000 polyethylene and 65 wt% of Mv of 950,000 polyethylene was dry-blended using a roll mixer to obtain Polyolefin composition. The obtained 30% by weight of the composition and 70% by weight of the liquid stone soil were uniformly melt-kneaded by a twin-screw extruder to obtain a polyethylene melt kneaded product. The melt-kneading conditions were as follows, the set temperature was 123124.doc -28 - 200831278 200 C, the number of screw revolutions was 170 rpm, and the discharge amount was 15 kg/hr. Then, the melt kneaded material was held at 22 (rCiT mold (width: 25 〇mm), and the melt kneaded material was extruded into a sheet shape. The molten kneaded material was pressed using a metal roll whose surface temperature was controlled to 60 ° C. 'And cooling it, thereby obtaining a gel sheet having a thickness stability of 1 〇〇〇μχη. Then using a simultaneous biaxial stretching machine at an extension temperature of 125. 〇 extends to 7x7 times 'and then' It is introduced into a methyl ethyl ketone tank, filled with methyl ethyl ketone for secondary collapse, and extracted to remove liquid paraffin. Thereafter, it is dried to remove methyl ethyl ketone. The inlet surface is stretched by using a tenter stretching machine. 〗2〇.〇 Extension 1 · 5 times, heat-fixed at 125 ° C, to obtain a microporous membrane with a lateral width of 12 m, a film thickness of 18 μηη, a porosity of 40%, and a pore diameter of 〇·〇5 μιη Further, the dynamic friction coefficient of the microporous film in the TD direction is 〇.4 [Production of the polyolefin microporous film wound material] In order to make the microporous film made of polysulfonated hydrocarbon finely cut into a plurality of strips Tension control can be performed separately on a plurality of cores, and in separate volumes "In the 卩 Χ 张力 tension detector, by which the tension of each finely cut polysulfide microporous membrane can be separately detected, and the output torque of each driving source is controlled according to the detected value. Using a separate driving slitter, The prepared polyolefin microporous film was cut into a width of 60 mm, and wound around a paper tube (size: 3 Å) to obtain a polyolefin microporous film wound. The d and L were 102 mm, respectively. 1000 m. Cut 8 mother rolls to make a IO60 roll of polyolefin microporous film winding, 123124.doc -29- 200831278. Extract from it, measure and calculate T to be 17.6~18·1 to produce more than 5 mm The winding offset winding has only one roll of 150 rolls with a winding offset of less than 5 mm, and the result is D·T, T, 1 The maximum value is 1·2μιη, the standard deviation is F(5), the average value is 25 N, F(10)_F(2〇)i is the average value μπι, and t is 17~19 0·4 μπι 〇 1 Ν. Furthermore, the cutting width of the cutting machine is set relative to the total width of the mother roll ^ m '

力為100N,並將寬度為6〇mm之各捲繞物之張力均控制 5 N 〇 … [電極•隔離膜捲繞物之製作·評估] 根據(3)之電極•隔離膜捲繞物之製作,製作岀電極•隔離 膜捲繞物,繼而,根據(4)電極•隔離膜捲繞物之外殼插入 性進行評估,結果為,不良品為〇,視為最佳。 [比較例1] 使用同軸切條機,將實施例i中所製作之聚烯烴製微多 孔膜切割成寬60 mm,並捲繞於管(尺寸等:3B)上,從而 獲得聚烯烴製微多孔膜捲繞物。d、L分別為ι〇2 _、 10 0 0 m 〇 切割9根母輥,製造出180卷聚烯烴製微多孔膜捲繞物, 產生5 mm以上之捲繞偏移之捲繞物有12卷。抽取15〇卷之 捲繞偏移為5 mm以内之捲繞切割物,測量並叶算D、τ、 t,其結果為:])為180.2〜183.9 mm,丁為17 2〜18 5叫、丈 為μιη,lT_tl之最大值為h6 μιη,標準偏差為〇 8 μπι 〇 123124.doc -30- 200831278 再者,本比較例中所使用之所謂同轴切條機係指,將切 割後之網狀物交替分開,且一併捲取於固定於具有旋轉驅 ‘ 動部之2根旋轉轴上的複數個卷芯上者。相對於母輥之總 、 寬度1 ·2 m,没切條機之抽取張力為1 〇〇 N,相對於各旋轉 轴,捲繞物之捲取張力為50 N,並不分別對每一捲繞物進 ' 行捲取張力控制。 - 以與實施例1相同之方式評估捲繞物外殼插入性,其結 果,產生3卷不良,視為不佳。 W [實施例2] [聚烯烴製微多孔膜之製作] 使用輥攪拌機,將35重量。/0之Mv為27萬之聚乙嬌、盥 重篁%2Μν為95萬之聚乙烯的混合物乾混和,從而獲得聚 烯烴組合物。藉由雙軸擠出機,對所獲得之3〇重量%之組 合物及70重量%之液體石蠟進行均一之熔融混練,從而獲 得聚乙烯熔融混練物。熔融混練條件如下,設定溫度為 ❿ 2〇〇°C、螺桿轉數為170 rpm、喷出量為15 kg/hr。繼而, 對熔融混練物使用保持於22〇t:iT塑模(寬度為25〇 mm), 將溶融混練物擠出成片狀。 . 使用表面溫度控制為6〇°C之金屬輥,對熔融混練物進行 •. 壓著,並使其冷卻,藉此,獲得厚度為1100 μηΐ2厚度穩 、 定性優異的凝膠片材。 、、璧而,使用同時雙軸延伸機,於延伸溫度延伸至 7X7倍,繼而,導入至曱基乙基酮槽中,於甲基乙基酮中 充分浸潰’萃取去除液體石躐,其後,乾燥去除甲基乙基 123124.doc -31- 200831278The force is 100N, and the tension of each winding with a width of 6〇mm is controlled to 5 N 〇... [Preparation and evaluation of electrode/separator winding] Electrode according to (3) • Coil winding The crucible electrode and the separator winding were produced, and then evaluated according to (4) the outer casing insertion property of the electrode/separator winding, and as a result, the defective product was 〇, which was regarded as the best. [Comparative Example 1] The polyolefin microporous film produced in Example i was cut into a width of 60 mm using a coaxial slitter, and wound on a tube (size: 3B) to obtain a polyolefin micro Porous film winding. d, L are ι〇2 _, 10 0 0 m 〇 cut 9 mother rolls, and make 180 rolls of polyolefin microporous film windings, resulting in a winding offset of 5 mm or more. volume. The winding cut of 15 windings with a winding offset of less than 5 mm is taken, and D, τ, and t are measured, and the result is:]) is 180.2~183.9 mm, Ding is 17 2~18 5, The maximum value of lT_tl is h6 μιη, and the standard deviation is 〇8 μπι 〇123124.doc -30- 200831278 Furthermore, the so-called coaxial cutting machine used in this comparative example refers to the net after cutting. The objects are alternately separated and wound together on a plurality of winding cores fixed to two rotating shafts having a rotary drive portion. With respect to the total width of the mother roll and the width of 1 · 2 m, the extraction tension of the slitter is 1 〇〇 N, and the winding tension of the winding is 50 N with respect to each rotating shaft, not for each roll. Winding into the 'winding tension control. - The insert casing outerness was evaluated in the same manner as in Example 1, and as a result, 3 rolls of defects were produced, which was considered to be poor. W [Example 2] [Production of polyolefin microporous film] Using a roll mixer, 35 weight was used. The Mv of /0 is dry blended with a mixture of polyethylene of 270,000, and 聚乙烯%2Μν of 95,000, thereby obtaining a polyolefin composition. The obtained 3% by weight of the composition and 70% by weight of the liquid paraffin were uniformly melt-kneaded by a twin-screw extruder to obtain a polyethylene melt-kneaded product. The melt kneading conditions were as follows, the set temperature was ❿ 2 〇〇 ° C, the number of screw revolutions was 170 rpm, and the discharge amount was 15 kg / hr. Then, the melt kneaded product was held in a 22 〇t:iT mold (having a width of 25 〇 mm), and the melt kneaded product was extruded into a sheet shape. Using a metal roll whose surface temperature is controlled to 6 ° C, the melt-kneaded material is pressed and cooled, thereby obtaining a gel sheet having a thickness of 1100 μη 2 and a stable and qualitative property. And, using a simultaneous biaxial stretching machine, extending to a temperature of 7×7 times at an extension temperature, and then introducing into a mercaptoethyl ketone tank, fully dipping in methyl ethyl ketone to extract and remove liquid sarcophagus, After drying, remove methyl ethyl 123124.doc -31- 200831278

進而,使用拉幅延伸機,沿橫方向於120°C延伸1·5倍, 於125°C進行熱固定,獲得橫向寬度為1·2 m、膜厚為20 μπι、空隙率為40%、孔徑為0·05 μπι之微多孔膜。又,微 多孔膜之TD方向之動摩擦係數為0.4。 [聚烯烴製微多孔膜捲繞物之製作] 使用單獨驅動切條機,將藉由上述方法鼓作之聚烯烴製Further, using a tenter stretching machine, it was extended by 1.5 times in the transverse direction at 120 ° C, and heat-fixed at 125 ° C to obtain a lateral width of 1.2 m, a film thickness of 20 μm, and a void ratio of 40%. A microporous membrane having a pore diameter of 0·05 μm. Further, the dynamic friction coefficient of the microporous film in the TD direction was 0.4. [Production of Polyolefin Microporous Film Winding] Using a separate driving slitter, a polyolefin made by the above method was used.

微多孔膜切割成寬60 mm,並捲繞於塑料製管(尺寸等: 6B)上,獲得聚烯烴製微多孔膜捲繞物。d、l分別為15〇 mm、10〇〇 m 〇 切割8根母輥8,製造出160卷 物,產生5 mm以上之捲繞偏移之捲繞物有2卷。抽取15〇卷 之捲繞偏移為5 mm以内之捲繞切割物,測量並計算β、 T、t,其結果為·· D為 216 2〜219 3 mm,丁為 19 〇〜] μΠ1、丨為19.7〜Μ叫1,lT_t|之最大值為1·4 ,標準偏差 為〇.3 μιη。又,F(5)之平均值為% N、f(1〇)_f㈣之平 值為0.9 N 〇 再者,相對於母輥之總寬度1>2 m,設切條機之抽取張 力為100 N,將60 mm寬之各捲繞物之張力均控制為5 N。 [電極•隔離膜捲繞物之製作·評估] ' 根據⑺之電極·隔離膜捲繞物之製作, 隔離膜捲繞物,繼而,根據⑷電極•隔離膜 外二 插入性進行評估,其結果為,不良品為卜視為良好。 [比較例2] 123124.doc -32 - 200831278 使用同軸切條機,將實施例2中所製作之聚烯烴製微多 孔膜切割成寬60 mm,並捲繞於管(尺寸等;6B)上,從而 獲得聚烯烴製微多孔膜捲繞物,d、L分別為150 mm、 1000 in 〇 切割9根母輥,製造出180卷聚烯烴製微多孔膜捲繞物, 產生5 mm以上之捲繞偏移之捲繞物有8卷。抽取15 0卷之捲 繞偏移為5 mm以内之捲繞切割物,測量並計算d、τ、t, 其結果為:D為 215·5〜220.1 mm,T為 18.2〜20·7 μιη、t為 19.7〜21 μηι,| T_t |之最大值為19 μπι,標準偏差為〇 8 μιη 〇 再者’相對於母親之總見度1 · 2 m,設切條機之抽取張 力為100 N,相對於各旋轉轴,捲繞物之捲取張力為5〇 N,並不對每一捲繞物進行捲取張力控制。 以與實施例1相同之方式評估捲繞物外殼插入性,其結 果’產生3卷不良’視為不佳。 [實施例3] 將12.8重量%之]^^為27萬之聚乙烯、192重量%之1^^為 95萬之超高分子量聚乙烯、48重量%之鄰苯二甲酸二辛酯 (DOP)、20重量。/。之微粉二氧化矽混合造粒後,使用前端 安裝有T塑模之雙軸擠出機熔融混練,之後擠出,藉由自 兩侧加熱後之輥進行壓延,形成為厚度為11〇 μπΐ2片狀。 自該成型物萃取去除膽、微粉二氧切,製作出微多孔 膜。重疊2片該微多孔膜,於11(rc沿縱方向延伸45倍,之 後’於133。(:沿橫方向延伸1>7倍,最後,於135。〇進行熱處 123124.doc -33· 200831278 理。獲得橫向寬度為1·2 m、膜厚為18 μηι、空隙率為 50%、孔徑為〇·ι μπι之微多孔膜。又,微多孔膜之TD方向 之動摩擦係數為0.2。 [聚烯烴製微多孔膜捲繞物之製作] 使用單獨驅動切條機’將藉由上述方法製作之聚烯烴製 微多孔膜切割成寬60 mm,並捲繞於塑料製管(尺寸等: 3B)上,從而獲得聚烯烴製微多孔膜捲繞物。d、乙分別為 102mm、10 0 0 m 〇 切割8根母輥,製造出160卷聚烯烴製微多孔膜捲繞物, 產生5 mm以上之捲繞偏移之捲繞物有2卷。抽取卷之捲 繞偏移為5 mm以内之捲繞切割物,測量並計算D、T、言, 其結果為:D為 18 1.2〜183.2 mm,T為 17.6〜18·2 μηι、t為 17〜19 μιη,|T_t|之最大值為i.3㈣,標準偏差為〇5 μηι。又,F(5)之平均值為25 N,F(1〇)_F(2〇)之平均值為2 N 〇 再者’相對於母親之總寬度i.2历寬,設切條機之抽取 張力為100 N,將60 mm寬之各捲繞物之卷芯張力均控制為 5 N 〇 [電極•隔離膜捲繞物之製作·評估] 根據(3)之電極•隔離膜捲繞物之製作,製作出電極•隔離 膜捲繞物,繼而,根據(4)電極•隔離膜捲繞物之外殼插入 性進行評估,其結果’不良品為i,視為良好。 [比較例3] 將丨2重量%iMv為200萬之超高分子量聚乙稀、12重量 123124.doc -34- 200831278 %2Mv為15萬之高密度聚乙烯、16重量%2Mv為15萬之直 鏈狀低密度聚乙烯、42.4重量%之鄰苯二甲酸二辛醋 * (DOP)、17.6重量%之微粉二氧化矽混合造粒後,使用安裝 ^ 有T塑模之雙軸擠出機混練•擠出,形成為厚度為9〇 μπι< 片狀。自該成形物萃取去除DOP及微粉二氧化矽,形成微 多孔膜。重疊2片該微多孔膜,於加熱至11 §之條件下, , 沿縱方向延伸5.3倍(延伸速度為1〇〇〇%/秒),之後,沿橫方 向延伸1·8倍(延伸速度為2%/秒)。獲得橫向寬度為〇.96 πι、膜尽為22 μπι之被多孔膜。又,微多孔膜之Td方向之 動厚擦係數為(Κ7。 使用同軸切條機,將所獲得之聚烯烴製微多孔膜切割赤 寬 60 mm。d、L分別為 1〇2 mm、1〇〇〇 m。 切割11根母輥,製造出176卷之聚烯烴製微多孔膜捲繞 物,產生5 mm以上之捲繞偏移之捲繞物有4卷。抽取15〇卷 之捲繞偏移為5 mm以内之捲繞切割物,測量並計算d、 • 丁、^其結果為:1>為 193 〜200 mm,T為 21.1〜23·2 μιη、t 為21·5〜23·8 μιη ’ I T-t I之最大值為ι ·6 μπι,標準偏差為 0.8 μιη ο ' 再者,相對於母輥之總寬度G.96 m寬,設切條機之抽取 •- 張力為80 N,且使相對於各旋轉轴,捲繞物之捲取張力為 • 40 N,並不對每一捲繞物進行捲取·張力控制。The microporous film was cut into a width of 60 mm and wound around a plastic tube (size: 6B) to obtain a polyolefin microporous film wound. d, l are 15 〇 mm, 10 〇〇 m 〇 respectively, and 8 mother rolls 8 are cut to produce 160 rolls, and there are 2 rolls of windings which produce a winding offset of 5 mm or more. The winding cut of 15 windings with a winding offset of 5 mm or less was taken, and β, T, and t were measured and calculated. The result was 216 2 to 219 3 mm, and D is 19 〇~] μΠ1. The maximum value of 19.7~Μ1, lT_t| is 1·4, and the standard deviation is 〇.3 μιη. Further, the average value of F(5) is % N, f(1〇)_f (four) is equal to 0.9 N 〇, and the total width of the mother roll is 1 > 2 m, and the extraction tension of the slitter is 100. N, the tension of each winding of 60 mm width is controlled to 5 N. [Preparation and evaluation of the electrode/separator winding material] The production of the electrode/spacer winding according to (7), the separator winding, and then the evaluation of the (4) electrode/spacer outer insertion property, the result For the bad goods, it is considered good. [Comparative Example 2] 123124.doc -32 - 200831278 The polyolefin microporous film produced in Example 2 was cut into a width of 60 mm using a coaxial slitter and wound on a tube (size, etc.; 6B). In order to obtain a polyolefin microporous film winding, d and L were cut into 9 mother rolls of 150 mm and 1000 in, respectively, and 180 rolls of polyolefin microporous film windings were produced to produce rolls of 5 mm or more. There are 8 rolls of winding around the offset. The wound cuts with a winding offset of 5 mm or less were taken, and d, τ, and t were measured and calculated. The result was: D was 215·5 to 220.1 mm, and T was 18.2 to 20·7 μηη. t is 19.7~21 μηι, | T_t | has a maximum value of 19 μπι, the standard deviation is 〇8 μιη 〇 and then the total relative to the mother is 1 · 2 m, and the extraction tension of the slitter is 100 N. The winding tension of the winding is 5 〇N with respect to each of the rotating shafts, and the winding tension control is not performed for each of the windings. The winding outer casing insertability was evaluated in the same manner as in Example 1, and the result 'produces 3 rolls of defects' was considered to be poor. [Example 3] 12.8% by weight of polyethylene was 270,000, 192% by weight of 1 ^^ was 950,000 ultrahigh molecular weight polyethylene, and 48% by weight of dioctyl phthalate (DOP) ), 20 weight. /. After the fine powder of cerium oxide is mixed and granulated, it is melt-kneaded by a twin-screw extruder equipped with a T-die at the front end, and then extruded, and rolled by a roller heated from both sides to form a thickness of 11 〇μπΐ2 pieces. shape. The bile and the micro-powder were removed by extraction from the molded product to prepare a microporous membrane. Two microporous membranes were overlapped, and 11 (rc extended 45 times in the longitudinal direction, then 'at 133. (: 1 in the transverse direction) 7 times, and finally, 135. The heat was 123124.doc-33· 200831278. A microporous membrane having a lateral width of 1.2 m, a film thickness of 18 μm, a porosity of 50%, and a pore diameter of 〇·ι μπι was obtained. Further, the dynamic friction coefficient of the microporous membrane in the TD direction was 0.2. Production of polyolefin microporous film wound material] The polyolefin microporous film produced by the above method was cut into a width of 60 mm and wound around a plastic tube (size: 3B) using a separate driving slitter On the basis of this, a polyolefin microporous film winding was obtained. d and B were 102 mm and 100 mm, respectively, and 8 mother rolls were cut to produce 160 rolls of polyolefin microporous film winding, resulting in 5 mm. The winding of the above winding offset has 2 rolls. The winding of the unwinding roll is offset within 5 mm, and the D, T, and D are measured and calculated. The result is: D is 18 1.2~183.2 Mm, T is 17.6~18·2 μηι, t is 17~19 μιη, the maximum value of |T_t| is i.3 (four), and the standard deviation is 〇5 μηι. The average value of F(5) is 25 N, and the average value of F(1〇)_F(2〇) is 2 N. Furthermore, the total width of the mother's width is i.2, and the extraction tension of the cutting machine is set. For 100 N, the core tension of each winding of 60 mm width is controlled to 5 N 〇 [Production and evaluation of electrode and separator winding] According to (3) Electrode • Separator winding The electrode/separator winding was produced, and then evaluated according to (4) the outer casing insertion property of the electrode/separator winding, and the result was that the defective product was i, which was considered to be good. [Comparative Example 3] 2% by weight iMv is 2 million ultra-high molecular weight polyethylene, 12 weight 123124.doc -34- 200831278 %2Mv is 150,000 high density polyethylene, 16% by weight 2Mv is 150,000 linear low density polyethylene 42.4% by weight of phthalic acid dioctyl vinegar* (DOP) and 17.6% by weight of fine powder of cerium oxide were mixed and granulated, and then mixed and extruded using a twin-screw extruder equipped with a T-die, and formed into The thickness is 9〇μπι< sheet shape. The DOP and the fine powder of cerium oxide are extracted and removed from the shaped product to form a microporous film. The two microporous membranes are overlapped and heated. Under the condition of 11 §, it extends 5.3 times in the longitudinal direction (extension speed is 1〇〇〇%/second), and then extends 1.8 times in the lateral direction (extension speed is 2%/second). 〇.96 πι, the membrane is a porous membrane of 22 μπι. Further, the dynamic thickness coefficient of the microporous membrane in the Td direction is (Κ7. The obtained polyolefin microporous membrane is cut by a coaxial slitting machine. 60 mm wide. d and L are 1〇2 mm and 1〇〇〇 m, respectively. Nineteen master rolls were cut to produce 176 rolls of polyolefin microporous film winding, and four windings were produced which produced a winding offset of 5 mm or more. Extract the 15 mm roll winding with a winding offset of less than 5 mm, measure and calculate d, • D, and ^. The result is: 1 > 193 ~ 200 mm, T is 21.1~23 · 2 μιη, t The maximum value of 21·5~23·8 μιη ' I Tt I is ι ·6 μπι, the standard deviation is 0.8 μιη ο ' Furthermore, the width of the mother roll is G.96 m wide, and the slitter is set. Extraction • The tension is 80 N, and the winding tension of the winding is • 40 N with respect to each rotating shaft, and the winding and tension control is not performed for each winding.

以與實施例1相同之方式評估捲繞物外殼插入性,產生5 卷不良^視為不佳DEvaluation of the insertability of the winding shell in the same manner as in Example 1, resulting in 5 rolls of defects ^ was regarded as poor D

[實施例4] 123124.doc -35- 200831278 將14·4重量%2Μν為27萬之聚乙烯、9 6重量%之Mv為 300萬之超咼分子量聚乙烯、56重量%之鄰苯二甲酸二辛 酯(DOP)、20重量%之微粉二氧化矽混合造粒後,使用前 端安裝有Τ塑模之雙軸擠出機熔融混練,之後擠出,藉由 自兩側加熱後之輥進行壓延,形成為厚度為丨1〇 μιη之片 狀。自該成形物萃取去除DOP、微粉二氧化矽,而製作出 微多孔膜。將該微多孔膜於115。〇沿縱方向延伸5·5倍後, 最後於120°C進行熱處理。獲得橫向寬度為〇·96 m、膜厚為 30 μιη、空隙率為70%、孔徑為〇·ι μιη之微多孔膜。md之 拉伸強度為190 MPa、TD之拉伸強度為18 MPa,(MD拉伸 強度/TD拉伸強度)之比為1 〇·6。又,微多孔膜之TD方向之 動摩擦係數為0.5。 [聚烯烴製微多孔膜捲繞物之製作] 使用單獨驅動切條機,將藉由上述方法製作之聚烯烴製 微多孔膜切割成寬6〇 mm,並捲繞於塑料製管(尺寸等: 3B)上’獲得聚烯烴製微多孔膜捲繞物。d、l分別為1〇2 mm、1000 Hi 〇 切割11根母輥,製造出176卷之聚稀烴製微多孔膜捲繞 物’產生5 mm以上之捲繞偏移之捲繞物有2卷。抽取150卷 之捲繞偏移為5 mm以内之捲繞切割物,測量並計算D、 丁、士’其結果為:〇為214.2〜2241!1111、1'為27.9〜31.20111、 t為28.2〜32·5 μπι,| T-t|之最大值為1·4 μπι,標準偏差為 〇·5 μπι。又,F(5)之平均值為25 N、F(1〇)_F(2〇)之平均值 為2 N。 123124.doc -36- 200831278 [電極•隔離膜捲繞物之製作·評估] 根據(3)之電極•隔離膜捲繞物之製作,製作出電極•隔離 膜捲繞物,繼而,根據⑷電極•隔離膜捲繞物之外殼插入 性進行評估,其結果,不良品為1,視為良好。 [聚烯烴製微多孔膜捲繞物受異物之損壞容易度之評估] 準備1根母輥,使用圖2所示之外徑测量器,於母輥之寬 度方向測量外徑,並料徑值最大處附近標註記號。繼 而,與上述聚烯烴製微多孔膜捲繞物之製作同樣地,切割 該母輥,捲繞所切割出之各聚烯烴微多孔膜,並於捲繞有 100 m時,向自標記有記號處附近所抽取之聚烯烴微多孔 膜所捲繞形成之捲繞物中,插入預先準備之〇1 mm見方之 氧化銘切片’並繼續切割。捲取i 〇〇〇茁後,解開捲繞物, 觀察因氧化鋁切片而產生之聚烯烴製微多孔膜之孔的開孔 狀態,可發現,有開孔縱貫2層。 [比較例4] 使用同轴切條機,將實施例4中所製作之聚烯烴製微多 孔膜切割成寬60 mm。d、L分別為1 〇2 mm、1 〇〇〇 m。 切割11根母輥,製造出176卷之聚烯烴製微多孔膜捲繞 物’產生5 mm以上之捲繞偏移之捲繞物有8卷。抽取150卷 之捲繞偏移為5 mm以内之捲繞切割物,測量並計算D、 T、t,其結果為:d 為 214.5〜223_5 mm,T 為 28.0〜31·〇 123124.doc -37- 200831278 μιη、t為28.2〜32.5 μηι,I T-t I之最大值為1.9 μιη,標準偏 差為 0.5 μπι。 再者,相對於母輥之總寬度0.96 m寬,設切條機之抽取 張力為8 0 N ’且使捲繞物相對於各旋轉轴之捲取張力為4 〇 N,並不對每一捲繞物進行捲取張力控制。 以與實施例4相同之方式評估捲繞物外殼插入性,其結 果,產生10卷不良,視為不佳。又,以與實施例4相同之 方式’對聚烯烴微多孔膜捲繞物受異物之損壞容易度進行 評估,其結果,發現有開孔縱貫5層。 [產業上之可利用性] 根據本發明之聚烯烴製微多孔膜捲繞物及其製造方法, 可提供一種減少了插入外殼時之插入不良的電極•隔離膜 一體型捲繞物’故而可較好地用於電池用隔離膜,尤其是 可較好地用於大型之鋰離子二次電池。 【圖式簡單說明】 圖1係表示本發明之捲繞物之外徑的測量裝置之一例的 概略圖。 圖2係表示本發明之捲繞物群之外徑的測量裝置之一例 的概略圖。 圖3係表示對複數個捲繞物同時進行尺寸測量之結果之 一例的線圖。 圖4係本發明之製造方法之一例之捲取臂的概略圖。 圖5係表示本發明之製造方法之一例的概略圖。 圖6係表示測量微多孔膜之膜厚之機構之基本構成部分 123124.doc -38- 200831278 的模式圖。 圖7係表示較好之膜厚測量裝置之模式圖(前視圖)。 圖8係表示較好之膜厚測量裝置之模式圖(前視圖)。 圖9係表示捲繞物之鬆緊度測量裝置之一例的模式圖 【主要元件符號說明】 1A 光學尺寸測量機之投影機 - 1B 光學尺寸測量機之受光機 2 聚烯烴製微多孔膜捲繞物 響 3 信號處理部 5 檢查結果輸出部 6 驅動傳送部 7 正時皮帶 8 管夾頭部 9 驅動軸 10 齒輪 • 11 母輥 12 聚烯烴製微多孔膜捲繞物 13 單獨臂部 • 14 切割器 … 21 支持台 22 支柱 23 試料台 24 測量端子桿 25 測量端子桿手動上下指示桿 123124.doc -39- 200831278 26 27 ^ 28 • 29 30 ^ 31 - 32 37 ❿ 類比顯示部 端子平行度調整構件 承壓調整部 光學偵測部固定部 光學偵測部 光學偵測部固定部高度調整部 承壓調整部固定部 試料 123124.doc -40-[Example 4] 123124.doc -35- 200831278 144.0% by weight of 2Μν was 270,000 parts of polyethylene, 96% by weight of Mv was 3 million of ultra-molecular weight polyethylene, 56% by weight of phthalic acid After dioctyl ester (DOP) and 20% by weight of fine powder of cerium oxide are mixed and granulated, they are melt-kneaded using a twin-screw extruder equipped with a ruthenium mold at the front end, and then extruded, by a roller heated from both sides. Calendering is formed into a sheet having a thickness of 丨1〇μηη. The DOP and the fine powder of cerium oxide were extracted and removed from the molded product to prepare a microporous film. The microporous membrane was at 115. After the crucible was extended 5 to 5 times in the longitudinal direction, the heat treatment was finally performed at 120 °C. A microporous membrane having a lateral width of 〇·96 m, a film thickness of 30 μm, a porosity of 70%, and a pore diameter of 〇·ι μιη was obtained. The tensile strength of md is 190 MPa, the tensile strength of TD is 18 MPa, and the ratio of (MD tensile strength / TD tensile strength) is 1 〇·6. Further, the dynamic friction coefficient of the microporous film in the TD direction was 0.5. [Production of Polyolefin-Based Microporous Film Winding] The polyolefin microporous film produced by the above method was cut into a width of 6 mm and wound around a plastic tube (size, etc.) using a separate driving slitter. : 3B) Upper 'obtained polyolefin microporous film winding. d, l are 1〇2 mm, 1000 Hi 〇 cut 11 mother rolls, and 176 rolls of micro-porous micro-porous film windings are produced, and the windings that produce a winding offset of 5 mm or more are 2 volume. Extract 150 windings with a winding offset of less than 5 mm, measure and calculate D, D, and Shi'. The result is: 〇 is 214.2~2241! 1111, 1' is 27.9~31.20111, t is 28.2~ The maximum value of 32·5 μπι,| Tt| is 1·4 μπι, and the standard deviation is 〇·5 μπι. Further, the average value of F(5) is 25 N, and the average value of F(1〇)_F(2〇) is 2 N. 123124.doc -36- 200831278 [Preparation and evaluation of the electrode/separator winding material] According to the production of the electrode/separator winding of (3), an electrode/separator winding is produced, and then, according to the (4) electrode • The outer casing insertability of the separator winding was evaluated, and as a result, the defective product was 1, which was considered to be good. [Evaluation of the ease of damage of foreign materials by the polyolefin microporous film winding] One mother roll was prepared, and the outer diameter was measured in the width direction of the mother roll using the outer diameter measuring device shown in Fig. 2, and the diameter value was measured. Mark the mark near the maximum. Then, similarly to the production of the above-mentioned polyolefin microporous film wound, the mother roll was cut, and the cut polyolefin microporous film was wound, and when it was wound 100 m, the self-marking was marked. In the winding formed by winding the polyolefin microporous membrane taken near the place, insert the previously prepared 氧化 1 mm square oxidized section ' and continue cutting. After the coil was taken up, the wound material was unwound, and the pore state of the pores of the polyolefin microporous membrane produced by the alumina slicing was observed, and it was found that the openings were two layers. [Comparative Example 4] The polyolefin microporous film produced in Example 4 was cut into a width of 60 mm using a coaxial slitter. d and L are 1 〇 2 mm and 1 〇〇〇 m, respectively. 11 mother rolls were cut to produce 176 rolls of polyolefin microporous film windings, and 8 windings were produced which produced a winding offset of 5 mm or more. Extract 150 pieces of winding cut with a winding offset of less than 5 mm, measure and calculate D, T, and t. The result is: d is 214.5~223_5 mm, T is 28.0~31·〇123124.doc -37 - 200831278 μιη, t is 28.2~32.5 μηι, I Tt I has a maximum value of 1.9 μηη and a standard deviation of 0.5 μπι. Furthermore, the total width of the mother roll is 0.96 m wide, and the pulling tension of the slitter is 80 N ', and the winding tension of the winding relative to each rotating shaft is 4 〇N, not for each roll. The winding tension control is performed on the winding. The insert outer casing insertability was evaluated in the same manner as in Example 4, and as a result, 10 rolls of defects were produced, which was considered to be poor. Further, in the same manner as in Example 4, the polyolefin microporous film winding was evaluated for the ease of damage by foreign matter, and as a result, it was found that the openings were five layers. [Industrial Applicability] According to the polyolefin microporous film wound of the present invention and the method for producing the same, it is possible to provide an electrode/separator integrated winding which reduces insertion failure when inserted into a casing. It is preferably used for a separator for batteries, and is particularly preferably used for a large-sized lithium ion secondary battery. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing an example of a measuring device for the outer diameter of a wound material of the present invention. Fig. 2 is a schematic view showing an example of a measuring device for the outer diameter of the wound group of the present invention. Fig. 3 is a line diagram showing an example of results of simultaneous measurement of a plurality of windings. Fig. 4 is a schematic view showing a winding arm of an example of the manufacturing method of the present invention. Fig. 5 is a schematic view showing an example of a manufacturing method of the present invention. Fig. 6 is a schematic view showing a basic constitution of a mechanism for measuring the film thickness of a microporous film 123124.doc-38-200831278. Fig. 7 is a schematic view (front view) showing a preferred film thickness measuring device. Fig. 8 is a schematic view (front view) showing a preferred film thickness measuring device. Fig. 9 is a schematic view showing an example of a tightness measuring device for a wound material [Description of main components] 1A Optical size measuring machine projector - 1B Optical size measuring machine light receiving machine 2 Polyolefin microporous film winding Ring 3 Signal processing unit 5 Inspection result Output unit 6 Drive transmission unit 7 Timing belt 8 Pipe clamp head 9 Drive shaft 10 Gear • 11 Master roller 12 Polyolefin microporous film winding 13 Individual arm • 14 Cutter ... 21 Support table 22 Pillar 23 Sample stage 24 Measuring terminal rod 25 Measuring terminal rod Manual up and down indicator rod 123124.doc -39- 200831278 26 27 ^ 28 • 29 30 ^ 31 - 32 37 ❿ Analog display terminal parallelism adjustment member bearing Pressure adjustment portion optical detection portion fixing portion optical detection portion optical detection portion fixing portion height adjustment portion pressure adjustment portion fixing portion sample 123124.doc -40-

Claims (1)

200831278 十、申請專利範圍: 1 · 一種聚烯烴製微多孔膜捲繞物,其特徵在於:其係將聚 • 烯烴製微多孔膜捲繞於卷芯上所成之捲繞物,並且,根 • 據下述式(1)所计异出之膜厚Τ(μηι)與對一片所評估之膜 厚(μπι)之差(膜厚差)的絕對值(^叫為15 μιη以下, ^ T(pm)=7c(D2-d2)/4L (1) • (上述式(1)中’ D係指捲繞於卷芯上之包含多孔膜之捲繞 物的外徑(mm),d係指卷芯之外徑(mm),l係指捲繞物 ® 之卷長(m))。 2·如請求項1之捲繞物,其係藉由下述方式而製造··對捲 繞於母輥上之聚烯烴製微多孔膜,於其總寬度上將其切 割成特定寬度後,一面控制由切割成該特定寬度之各聚 烯烴製微多孔膜所捲成之各捲繞物的捲取張力,一面進 行捲繞。200831278 X. Patent application scope: 1 . A polyolefin microporous film wound product, which is characterized in that it is a wound formed by winding a polycrystalline olefin microporous film on a winding core, and • The absolute value of the difference between the film thickness Τ(μηι) calculated according to the following formula (1) and the film thickness (μπι) evaluated for one piece (^ is 15 μmη or less, ^ T (pm)=7c(D2-d2)/4L (1) • (In the above formula (1), 'D is the outer diameter (mm) of the wound containing the porous film wound around the core, d system The outer diameter (mm) of the winding core, and l is the winding length (m) of the winding material. 2. The winding of claim 1 is manufactured by the following method. The polyolefin microporous film on the mother roll is cut into a specific width over its entire width, and then controlled by each of the wounds of the polyolefin microporous film cut into the specific width Winding is performed while winding up. 如請求項1之捲繞物,其係藉由單獨驅動式切割機而切 割。 如請求項1至3中任一項之捲繞物,其中與卷芯相距5 mm 處之鬆緊度為34 N以下。 5·如請求項4之捲繞物,其中與卷芯相距1〇 mm處之鬆緊度 (F(l〇))、及與卷芯相距20 mm處之鬆緊度(F(2〇))的差 (F(10)-F(20))為 0·05Ν以上 2N以下。 6·如請求項1至3中任一項之捲繞物’其卷長為5〇〇mw 上。 7·如請求項1至3中任一項之捲繞物,其中聚烯烴製微多孔 123124.doc 200831278 膜之 孔徑為0·0Ό1 μπι以上1 μπι以下, 空隙率為25%以上75%以下, 膜厚為3 μπι以上200 μπι以下。 8·如請求項1至3中任一項之捲繞物,其中聚烯烴製微多孔 膜之寬度方向之動摩擦係數為0.6以下。The winding of claim 1 is cut by a separately driven cutter. The winding of any one of claims 1 to 3, wherein the tightness at 5 mm from the core is 34 N or less. 5. The winding of claim 4, wherein the tightness (F(l〇)) at a distance of 1 mm from the core and the tightness at a distance of 20 mm from the core (F(2〇)) The difference (F(10)-F(20)) is 0·05 Ν or more and 2N or less. 6. The wound article of any one of claims 1 to 3 having a roll length of 5 〇〇mw. The winding material according to any one of claims 1 to 3, wherein the polyolefin microporous 123124.doc 200831278 has a pore diameter of 0·0Ό1 μπι or more and 1 μπι or less, and a void ratio of 25% or more and 75% or less. The film thickness is 3 μπι or more and 200 μπι or less. The winding material according to any one of claims 1 to 3, wherein the polyolefin microporous film has a dynamic friction coefficient in the width direction of 0.6 or less. 9·如請求項1至3中任一項之捲繞物,其中聚烯烴製微多孔 膜之縱方向之拉伸強度(MD拉伸強度)與寬度方向之拉伸 強度(TD拉伸強度)之比(MD拉伸強度/TD拉伸強度)為10 以上。 I 〇·如請求項1至3中任一項之捲繞物,其用於電池周隔離 膜。 II ·如請求項1至3中任一項之捲繞物,其係用於電池用隔離 膜,並且, 聚烯烴製微多孔膜之 孔徑為0 · 〇 〇 1 μιη以上1 μπι以下, 空隙率為25%以上75%以下, 膜厚為3 μπι以上200 μηι以下。 12. —種聚烯烴製微多孔膜捲繞物群,其係包含2個以上之 使捲繞於母輥上<聚烯烴製微多孔膜切割所得之如請求 項1所述之捲繞物的捲繞物群’捲繞偏移為$ mm以 〇請求項!中所記載之膜厚差_的標準偏差⑽_ 13 · —種捲繞物群 其特徵在於 其係藉由下述方式而製造 123124.doc 200831278 之捲繞物群··對捲繞於母輥上之聚烯烴製微多孔膜,於 其總寬度上將其切割成特定寬度後,一面控制由切割成 該特定寬度之各聚烯烴製微多孔膜所構成之各捲繞物的 . 捲取張力,一面進行捲繞,並且,各捲繞物之捲繞偏移 為5 mm以内,且根據下述式(1)所計算出之各捲繞物之 膜厚Τ(μπι)與對一片所評估之膜厚《卜叫之差(膜厚差)的 ' 標準偏差為0 · 7 μιη以下, T(pm)=7i(D2_d2)/4L (1) (上述式中,D係指捲繞於卷芯上之包含多孔膜之捲繞物 的外徑(mm),d係指卷芯之外徑(mm),l係指捲繞物之 卷長(m))。 14·如請求項12之捲繞物群,其係藉由單獨驅動式切割機而 切割。 15·如請求項12至14中任一項之捲繞物群,其中各聚烯烴製 微多孔膜捲繞物之卷長為500 m以上。 • I6·如請求項12至14中任一項之捲繞物群,其中聚烯烴製微 多孔膜之 孔徑為0.001 μιη以上1 μιη以下, ^ 空隙率為25%以上75%以下, 膜厚為3 μπι以上2 0 0 μπι以下。 17. 如請求項12至14中任一項之捲繞物群,其用於電池用隔 離膜。 18. 如請求項12至14中任一項之捲繞物群,其係用於電池用 隔離膜,並且, 123124.doc 200831278 聚烯烴製微多孔膜之 孔控為0.001 μπι以上1 μπι以下, 空隙率為25%以上75%以下, 膜厚為3 μηι以上200 μπι以下。 19· 一種如請求項〗所述之捲繞物之製造方法,係使用單獨 驅動式切割機切割捲繞於母輥上之聚烯烴製微多孔膜從 而製造聚烯烴製微多孔膜捲繞物者,並且於母輥總寬度 上切刎出之捲繞偏移為5 mm以内的捲繞物群中,根據下 述式(1)所計算出之膜厚Τ(μιη)與對一片所評估之膜厚 Κμιη)之差(膜厚差)的標準偏差為〇7μιη以下, T(pm)=7i(D2 = d2)/4L (1) (上述式(1)中,D係指捲繞於卷芯上之包含多孔膜之捲繞 物的外徑(mm),以系指卷芯之外徑,[係指捲繞物 之卷長(m))。 2〇· —種聚烯烴製微多孔膜捲繞物之製造方法,包括以下步 驟: 將捲繞於母輥上之聚烯烴製微多孔膜,於其總寬度上 切割成特定寬度;以及 一面控制由切割成該特定寬度之各聚烯烴製微多孔膜 所構成之各捲繞物的捲取張力,一面進行捲繞。 21· —種聚烯烴製微多孔膜捲繞物之製造方法,包括以下步 驟: 將捲繞於母輥上之聚烯烴製微多孔膜,於其總寬度上 切割分離成特定寬度;以及 123124.doc 200831278 一面控制由切割成該特定寬度之各聚烯烴製微多孔膜 所構成之各捲繞物的捲取張力,一面進行捲繞;其中 該聚烯烴製微多孔膜捲繞物之捲繞偏移為5 mm以内, 且根據下述式(1)所計算出之膜厚Τ(μιη)與對一片所評估 出之膜厚ΐ(μπι)之差(膜厚差)的標準偏差為〇·7 μπχ以下, Τ(μπι)=π(ϋ2-(12)/4Ε (1) (上述式(1)中,D係指捲繞於卷芯上之包含多孔膜之捲繞 物的外徑(mm),d係指卷芯之外徑(mm),l係指捲繞物 之卷長(m))。 22. 如請求項20之製造方法,其中使用單獨驅動式切割機進 行切割。 23. 如請求項20之製造方法,其中根據下述式(1)所計算出之 聚烯烴製微多孔膜捲繞物之膜厚Τ(μηι)與對一片所評估 出之膜尽ΐ(μηι)之差(膜厚差)的絕對值(μηι)為1 ·5 μιη以 下, Tbm)=7i(D2-d2)/4L (1) (下述式(1)中,D係指捲繞於卷芯上之包含多孔膜之捲繞 物的外徑(mm),d係指卷芯之外徑(mm),l係指捲繞物 之卷長(m))。 24·如請求項19至23中任一項之製造方法,其中聚烯烴製微 多孔膜捲繞物之與卷芯相距5 mm處之鬆緊度為34 N以 下。 25.如請求項19至23中任一項之製造方法,其中與卷芯相距 10 mm處之鬆緊度(F(i〇))、及與卷芯相距2〇 mm處之鬆 123124.doc 200831278 緊度(F(20))的差(F(10)-F(20))為 0.05 N 以上 2 N 以下。 26.如請求項19至23中任一項之製造方法,其中聚烯烴製微 β 多孔膜捲繞物之卷長為500 m以上。 - 27·如請求項19至23中任一項之製造方法,其中聚烯烴製微 多孔膜之 孔徑為0.001 μπι以上1 μηι以下, 、 空隙率為25%以上75%以下, 膜厚為3 μιη以上200 μπι以下。 W 28·如請求項19至23中任一項之製造方法,其中聚烯烴製微 多孔膜之寬度方向之動摩擦係數為0.6以下。 29.如請求項19至23中任一項之製造方法,其中聚烯烴製微 多孔膜之縱方向之拉伸強度(MD拉伸強度)與寬度方向之 拉伸強度(TD拉伸強度)之比(MD拉伸強度/TD拉伸強度) 為10以上。 3 0.如請求項19至23中任一項之製造方法,其中聚烯烴製微 φ 多孔膜係電池用隔離膜。 31.如請求項19至23中任一項之製造方法,其中聚烯烴製微 多孔膜係電池用隔離膜,且聚烯烴製微多孔膜之 ' 孔徑為0.001 μιη以上1 μιη以下, . 空隙率為25%以上75%以下, 膜厚為3 μηι以上2 0 0 μπι以下。 123124.doc9. The wound material according to any one of claims 1 to 3, wherein tensile strength (MD tensile strength) in the longitudinal direction and tensile strength (TD tensile strength) in the width direction of the polyolefin microporous film The ratio (MD tensile strength / TD tensile strength) is 10 or more. I. The winding of any one of claims 1 to 3 for use in a battery separator. The winding material according to any one of claims 1 to 3, which is used for a separator for a battery, and the pore diameter of the polyolefin microporous film is 0 · 〇〇1 μm or more and 1 μπι or less, void ratio It is 25% or more and 75% or less, and the film thickness is 3 μπι or more and 200 μηι or less. 12. A polyolefin microporous film wound group comprising two or more windings as claimed in claim 1 which are obtained by cutting a polyolefin microporous film wound on a mother roll. The winding group 'winding offset is $ mm to request the item! The standard deviation (10) of the film thickness difference _ 13 described in the above-mentioned article is characterized in that it is manufactured by the following method: 123124.doc 200831278 The winding group is wound on the mother roll The polyolefin microporous film is cut into a specific width over the total width thereof, and then controlled by the winding tension of each of the polyolefin microporous films cut into the specific width. Winding is performed on one side, and the winding deviation of each winding is within 5 mm, and the film thickness Τ (μπι) of each of the wounds calculated according to the following formula (1) is evaluated The standard deviation of the film thickness "difference (difference in film thickness) is 0 · 7 μηη or less, T (pm) = 7i (D2_d2) / 4L (1) (in the above formula, D means winding around the core The outer diameter (mm) of the wound material including the porous film, d means the outer diameter (mm) of the core, and l means the coil length (m) of the wound. 14. The group of coils of claim 12 which is cut by a separately driven cutter. The winding group according to any one of claims 12 to 14, wherein each of the polyolefin microporous film wounds has a roll length of 500 m or more. The winding group according to any one of claims 12 to 14, wherein the polyolefin microporous membrane has a pore diameter of 0.001 μm or more and 1 μm or less, and a void ratio of 25% or more and 75% or less, and the film thickness is 3 μπι or more 2 0 0 μπι or less. 17. The coiled article of any one of claims 12 to 14 for use in a separator for a battery. 18. The winding group according to any one of claims 12 to 14, which is used for a separator for a battery, and the pore control of the polyolefin microporous membrane of 123124.doc 200831278 is 0.001 μπι or more and 1 μπι or less. The void ratio is 25% or more and 75% or less, and the film thickness is 3 μηι or more and 200 μπι or less. 19. A method of producing a wound material according to the above claim, wherein a polyolefin microporous film wound on a mother roll is cut by a separate driven cutter to produce a polyolefin microporous film winding. And the film thickness μ(μιη) calculated according to the following formula (1) and the evaluation of one piece in the group of windings with a winding deviation of 5 mm or less in the total width of the mother roll The difference in film thickness Κμιη) (standard deviation of film thickness) is 〇7μηη or less, T(pm)=7i(D2 = d2)/4L (1) (In the above formula (1), D is wrapped around a roll. The outer diameter (mm) of the wound material including the porous film on the core is referred to as the outer diameter of the core, and [refers to the winding length (m) of the wound). A method for producing a polyolefin microporous film wound, comprising the steps of: cutting a polyolefin microporous film wound on a mother roll into a specific width over a total width thereof; and controlling one side The winding is performed while winding up the tension of each of the wound materials of the polyolefin microporous film cut into the specific width. A method for producing a polyolefin microporous film wound, comprising the steps of: cutting a polyolefin microporous film wound on a mother roll to a specific width in a total width thereof; and 123124. Doc 200831278 Winding while controlling the winding tension of each of the wound materials composed of the polyolefin microporous membranes cut to the specific width; wherein the polyolefin microporous film winding is wound The standard deviation of the difference between the film thickness μ(μιη) calculated according to the following formula (1) and the film thickness ΐ(μπι) evaluated for one piece (difference in film thickness) is 〇· 7 μπχ or less, Τ(μπι)=π(ϋ2-(12)/4Ε (1) (In the above formula (1), D means the outer diameter of the wound containing the porous film wound on the core ( Mm), d is the outer diameter (mm) of the core, and l is the winding length (m) of the winding. 22. The manufacturing method of claim 20, wherein the cutting is performed using a separate driven cutter. The manufacturing method of claim 20, wherein the film thickness of the polyolefin microporous film winding is calculated according to the following formula (1) (μηι ) The absolute value (μηι) of the difference (μηι) between the film and the film (μηι) evaluated for one piece is 1 · 5 μηη or less, Tbm) = 7i (D2-d2) / 4L (1) (below In the above formula (1), D means the outer diameter (mm) of the wound containing the porous film wound on the core, d means the outer diameter (mm) of the core, and l means the winding Volume length (m)). The manufacturing method according to any one of claims 19 to 23, wherein the polyolefin microporous film winding has a tightness of 5 N or less from the core of the winding of 34 N or less. The manufacturing method according to any one of claims 19 to 23, wherein the tightness (F(i〇)) at a distance of 10 mm from the core and the looseness at a distance of 2 mm from the core are 123124.doc 200831278 The difference (F(10)-F(20)) of the tightness (F(20)) is 0.05 N or more and 2 N or less. The production method according to any one of claims 19 to 23, wherein the polyolefin micro-β porous film winding has a roll length of 500 m or more. The production method according to any one of claims 19 to 23, wherein the polyolefin microporous membrane has a pore diameter of 0.001 μπι or more and 1 μηι or less, a porosity of 25% or more and 75% or less, and a film thickness of 3 μm. Above 200 μπι. The manufacturing method according to any one of claims 19 to 23, wherein the polyolefin microporous film has a dynamic friction coefficient in the width direction of 0.6 or less. The production method according to any one of claims 19 to 23, wherein the tensile strength (MD tensile strength) in the longitudinal direction and the tensile strength (TD tensile strength) in the width direction of the polyolefin microporous film are The ratio (MD tensile strength / TD tensile strength) is 10 or more. The production method according to any one of claims 19 to 23, wherein the polyolefin is a separator for a micro φ porous membrane battery. The production method according to any one of claims 19 to 23, wherein the polyolefin microporous membrane is a separator for a battery, and the polyolefin microporous membrane has a pore diameter of 0.001 μm or more and 1 μm or less. It is 25% or more and 75% or less, and the film thickness is 3 μηι or more and 2 0 0 μπι or less. 123124.doc
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